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JP5238993B2 - Tea extract, tea beverage and method for producing them - Google Patents

Tea extract, tea beverage and method for producing them Download PDF

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JP5238993B2
JP5238993B2 JP2007314237A JP2007314237A JP5238993B2 JP 5238993 B2 JP5238993 B2 JP 5238993B2 JP 2007314237 A JP2007314237 A JP 2007314237A JP 2007314237 A JP2007314237 A JP 2007314237A JP 5238993 B2 JP5238993 B2 JP 5238993B2
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tea
extract
sample
catechins
enzyme
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JP2009095333A (en
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浩二 長尾
秀樹 牧
健 鈴木
芳明 横尾
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Suntory Beverage and Food Ltd
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Priority to JP2007314237A priority Critical patent/JP5238993B2/en
Priority to MYPI2010001308A priority patent/MY156443A/en
Priority to NZ584154A priority patent/NZ584154A/en
Priority to US12/679,743 priority patent/US20100272857A1/en
Priority to AU2008304863A priority patent/AU2008304863A1/en
Priority to EP08833261.4A priority patent/EP2193721B2/en
Priority to CA2704709A priority patent/CA2704709C/en
Priority to PCT/JP2008/067385 priority patent/WO2009041555A1/en
Priority to TW097137289A priority patent/TWI526159B/en
Priority to CN200880116986.1A priority patent/CN101932252B/en
Priority to ES08833261T priority patent/ES2657404T5/en
Publication of JP2009095333A publication Critical patent/JP2009095333A/en
Priority to HK11104586.9A priority patent/HK1150731A1/en
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/16Tea extraction; Tea extracts; Treating tea extract; Making instant tea
    • A23F3/163Liquid or semi-liquid tea extract preparations, e.g. gels, liquid extracts in solid capsules
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/16Tea extraction; Tea extracts; Treating tea extract; Making instant tea
    • A23F3/166Addition of, or treatment with, enzymes or microorganisms
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/16Tea extraction; Tea extracts; Treating tea extract; Making instant tea
    • A23F3/18Extraction of water soluble tea constituents
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/16Tea extraction; Tea extracts; Treating tea extract; Making instant tea
    • A23F3/20Removing unwanted substances

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dispersion Chemistry (AREA)
  • Microbiology (AREA)
  • Tea And Coffee (AREA)

Description

発明の属する技術分野TECHNICAL FIELD OF THE INVENTION

本発明は、茶抽出物、茶飲料及びそれらの製造方法に関し、特に茶の旨味成分であるアミノ酸を高濃度に含有し苦味・渋味成分であるカテキン類が除去された、嗜好性に優れた茶抽出物の製造方法に関する。   The present invention relates to tea extracts, tea beverages, and methods for producing the same, and in particular, it has excellent palatability, in which catechins that are bitter and astringent components are removed, containing amino acids that are umami components of tea in high concentrations. The present invention relates to a method for producing a tea extract.

従来技術Conventional technology

元来、緑茶は玉露のように茶葉から浸出されるアミノ酸の味が多いほど、良質の茶あるいは上手な抽出法として評価される。例えば、玉露を60℃程度の温度で抽出したり、また、通常の煎茶を氷水で抽出したりするのは渋味の多いカテキン類を抽出せずに旨味の成分だけを取り出すことに基づいている。即ち、香味の優れた緑茶とはカテキン含量が少なく、旨味が強いものであると、言われる事が多い。   Originally, green tea is evaluated as a good tea or better extraction method as the taste of amino acids leached from tea leaves like gyokuro increases. For example, extracting gyokuro at a temperature of about 60 ° C. or extracting ordinary sencha with ice water is based on extracting only umami components without extracting catechins with a lot of astringency. . That is, it is often said that green tea with excellent flavor has a low catechin content and a strong umami.

近年、缶やペットボトル等の容器に充填された容器詰茶飲料が多く開発されており、茶飲料のなかでも、特に緑茶飲料の市場が拡大している。このような茶飲料に対する消費者の嗜好は高まっており、急須で入れたような、旨味やコク味が強く、渋味や苦味が抑えられた容器詰茶飲料の開発が望まれている。   In recent years, many packaged tea beverages filled in containers such as cans and plastic bottles have been developed, and the market for green tea beverages is growing especially among tea beverages. Consumers' preference for such tea beverages is increasing, and there is a demand for the development of packaged tea beverages that have strong umami and richness and have reduced astringency and bitterness, as put in a teapot.

そこで、香味の豊かな茶抽出物または茶飲料の製造方法として、次のような方法が報告されている。特許文献1には、茶類から低温抽出水と高温抽出水の少なくとも2種類の抽出水にて有用成分を抽出することを特徴とする茶類の抽出方法が記載されている。緑茶の場合には、40〜60℃の低温抽出水で抽出するとアミノ酸、カテキン、カフェイン等の主に旨みあるいは渋み等の成分や比較的沸点の低いヘキサナール等の香気成分を抽出することができ、高温抽出水で抽出するとカテキン等の渋み成分を主に抽出することができることが記載されている。   Therefore, the following method has been reported as a method for producing a flavorful tea extract or tea beverage. Patent Document 1 describes a tea extraction method characterized in that useful components are extracted from teas with at least two types of extraction waters of low temperature extraction water and high temperature extraction water. In the case of green tea, extraction with low temperature extraction water at 40-60 ° C. can extract components such as umami or astringency such as amino acids, catechins and caffeine, and aromatic components such as hexanal having a relatively low boiling point. It is described that astringent components such as catechin can be mainly extracted when extracted with high temperature extraction water.

特許文献2には、茶葉を80〜100℃の高温水中で抽出後、30〜50℃の低温で抽出するという2段階抽出法による、高温抽出茶飲料と同程度の高い香りをもち、低温抽出茶飲料と同程度の深い旨味と強いコク、弱い渋みを有する茶飲料が開示されている。   In Patent Document 2, tea leaves are extracted in high temperature water at 80 to 100 ° C and then extracted at a low temperature of 30 to 50 ° C. Tea beverages having deep umami, strong richness and weak astringency similar to tea beverages are disclosed.

特許文献3には、緑茶葉を−5〜9℃の水で抽出した抽出液と、この抽出残渣を50〜100℃の温水で抽出した抽出液とを混合して得られる、カテキン類を高濃度に含有し強すぎる苦味や渋味を抑えた茶飲料が開示されている。   In Patent Document 3, catechins obtained by mixing an extract obtained by extracting green tea leaves with water at −5 to 9 ° C. and an extract obtained by extracting this extraction residue with warm water at 50 to 100 ° C. A tea beverage containing a too strong bitterness or astringency that is contained in the concentration is disclosed.

特許文献4には、溶存酸素が除去され且つ0〜36℃に保持されてなる静水中に茶葉を浸漬して抽出することで旨味を有するとともに渋みが少ない茶抽出液が得られることが開示されている。
特許文献5には、20℃以上60℃未満(好ましくは50℃以下)で、溶存酸素濃度1ppm以下の脱気水を用い、総カテキン類濃度及び没食子酸エステル型カテキン類濃度を特定範囲になるように抽出を行うことで、常温以下に冷却された状態で販売され飲用される場合の渋味や収歛味を抑えた茶飲料が製造できることが開示されている。
また、酵素を利用して抽出することにより、茶抽出物の風味を高める方法も開示されている。例えば、特許文献6には、普通の緑茶にタンニン分解酵素を添加混合し、熱水抽出することが記載されており、この効果として茶特有の風味が増強されることが記載されている。
特許文献7には、茶抽出液に除タンニン処理を施した後、グルタミナーゼを作用させて、茶抽出液中のグルタミン酸量を増加させることが開示されている。
特許文献8には、煎茶(緑茶)にプロトペクチナーゼ及びプロテアーゼを添加混合し、これを抽出処理し得られた抽出液が風味に優れたものであることが記載され、さらに、プロテアーゼが茶葉中の蛋白質を分解して、アミノ酸を生成させ、アミノ酸の風味により、抽出液の苦味、渋みなどを低減させる働きをすることも記載されている。
特許文献9には、茶類原料にプロテアーゼおよびタンナーゼの2種の酵素を添加して抽出することにより、両酵素が相互に作用し合って、それぞれの酵素の単独使用からは予測し得ない相乗的な効果を発揮し、旨味やコク味が強く、渋味の少ない高級感のある緑茶エキスを製造することができることが記載されている。
特許文献10には、セルラーゼ、ヘミセルラーゼ、ペクチナーゼ、およびプロトペクチナーゼを有する酵素群を用い、茶葉を酵素分解抽出処理することにより得られた高旨味茶葉抽出液と、高温抽出法で得た高温抽出茶葉抽出液とを用いた緑茶飲料の製造方法が開示されている。
さらに、アミノ酸を添加することにより、苦味や渋味を低減させた茶飲料も報告されている。例えば、特許文献11には、テアニン添加により苦味と渋味を低減させた半発酵茶が開示されている。本出願人らも、カテキンの含有量が40〜100mg/100mLである茶飲料に、グルタミン酸を6〜20mg/100mL添加してカテキンの渋味を抑制した茶飲料を開示している(特許文献12)。
特開平11−56242号公報 特開平6−303904号公報 特許第3590027号公報 特開2000−50799号公報 特開平6−343389号公報 特開昭49−110900号公報 特開2005−124500号公報 特開平1−300848号公報 特許第3782718号公報 特許第3820372号公報 特開2000−197449号公報 特開2006−42728号公報
Patent Document 4 discloses that a tea extract having umami and less astringency can be obtained by immersing and extracting tea leaves in still water from which dissolved oxygen is removed and maintained at 0 to 36 ° C. ing.
In Patent Document 5, degassed water having a dissolved oxygen concentration of 1 ppm or less at 20 ° C. or more and less than 60 ° C. (preferably 50 ° C. or less) is used, and the total catechin concentration and gallic acid ester type catechin concentration fall within a specific range. It is disclosed that by performing extraction as described above, it is possible to produce a tea beverage with reduced astringency and astringency when sold and drunk in a state cooled to room temperature or lower.
Moreover, the method of improving the flavor of a tea extract is also disclosed by extracting using an enzyme. For example, Patent Document 6 describes that tannin-degrading enzyme is added to and mixed with ordinary green tea and extracted with hot water, and this effect describes that the flavor unique to tea is enhanced.
Patent Document 7 discloses that after removing tannin from a tea extract, glutaminase is allowed to act to increase the amount of glutamic acid in the tea extract.
Patent Document 8 describes that an extract obtained by adding protopectinase and protease to sencha (green tea) and extracting the mixture is excellent in flavor, and further, protease is contained in tea leaves. It is also described that protein is decomposed to produce amino acids, and the amino acid flavor acts to reduce the bitterness, astringency and the like of the extract.
Patent Document 9 describes a synergistic effect that cannot be predicted from the single use of each enzyme by adding two types of enzymes, protease and tannase, to the tea material and extracting them. It is described that a green tea extract with a high-class feeling can be produced that exhibits a natural effect, has a strong umami taste and richness, and has little astringency.
Patent Document 10 discloses a high-flavored tea leaf extract obtained by enzymatic degradation extraction treatment of tea leaves using an enzyme group having cellulase, hemicellulase, pectinase, and protopectinase, and high-temperature extraction obtained by a high-temperature extraction method. A method for producing a green tea beverage using a tea leaf extract is disclosed.
Furthermore, tea beverages that have reduced bitterness and astringency by adding amino acids have also been reported. For example, Patent Document 11 discloses a semi-fermented tea in which the bitterness and astringency are reduced by adding theanine. Applicants have also disclosed a tea beverage in which 6-20 mg / 100 mL of glutamic acid is added to a tea beverage having a catechin content of 40-100 mg / 100 mL to suppress the astringent taste of catechin (Patent Document 12). ).
Japanese Patent Laid-Open No. 11-56242 JP-A-6-303904 Japanese Patent No. 3590027 JP 2000-50799 A JP-A-6-343389 JP 49-110900 A JP 2005-124500 A Japanese Patent Laid-Open No. 1-300848 Japanese Patent No. 3787718 Japanese Patent No. 3820372 JP 2000-197449 A JP 2006-42728 A

上記のとおり、茶抽出物中の風味を高める方法が種々知られており、酵素を利用して抽出する方法では、酵素が茶葉及び/又は茶抽出液中のタンパク質や繊維質に作用することにより、抽出液中の旨味成分であるアミノ酸濃度を高めることが知られている。しかし、これらの方法で得られる茶抽出物の風味は必ずしも十分に満足しうるものではなく、より旨味・コク味成分であるアミノ酸を高濃度に含有し、苦味・渋味成分であるカテキン類を低減させた茶抽出物の開発が望まれていた。
すなわち、本発明は、旨味・コク味成分を高濃度に含有し、苦味・渋味成分を低減させた茶抽出物およびその製造方法を提供することを目的とする。また、本発明は、豊かな旨味を有し渋味の少ない量販可能な容器詰茶飲料を提供することを目的とする。
As described above, various methods for enhancing the flavor in the tea extract are known. In the method of extracting using an enzyme, the enzyme acts on proteins and fiber in tea leaves and / or tea extract. It is known to increase the concentration of amino acids that are umami components in the extract. However, the flavor of the tea extract obtained by these methods is not always satisfactory, it contains a higher concentration of amino acids that are more umami and kokumi ingredients, and catechins that are bitter and astringent ingredients. Development of reduced tea extract has been desired.
That is, an object of the present invention is to provide a tea extract containing a umami / kokumi component at a high concentration and having reduced bitterness / astringency components and a method for producing the tea extract. Another object of the present invention is to provide a container-packed tea beverage that has a rich umami and can be sold in large quantities with little astringency.

本発明者らは、上記課題を解決するために鋭意検討した結果、酵素を利用して抽出を行う(本明細書中、「酵素抽出」と表記することもある)際に、酵素のアミノ酸濃度を高める作用がカテキン類の存在によって十分に発揮されない、又は阻害される、ことがあるとの考えに至った。この考えに基づき、茶葉からカテキン類の少なくとも一部を除去した後、この茶葉の酵素抽出を行うと、得られる茶抽出物のアミノ酸含量が飛躍的に高くなり、かつカテキン類含量が低減されることを見出した。そして、この茶抽出物が、従来にない組成を有すること、すなわち茶抽出物中の茶葉由来固形分に対し、アミノ酸の総量の割合が2.5重量%以上(好ましくは5.0重量%以上、より好ましくは7.0重量%以上)であり、カテキン類の総量の割合が15.0重量%以下(好ましくは13.5重量%以下、より好ましくは10.0重量%以下、特に好ましくは8.0重量%以下)であること、さらにこの茶抽出物が旨味・コク味を有し苦渋味を有さないことから、茶飲料の風味増強剤として利用可能であることを確認した。
また、本発明者らは、さらに検討を進めた結果、上記の茶抽出物にテアニンを一定量の割合で混合すると、フレッシュな旨味を付与することができることを見出した。そして、このテアニンとして茶葉の低温抽出液を用いると、フレッシュな旨みと厚みのあるコクを備え、苦味や渋味が低減された茶抽出物となること、特に、低温抽出液の抽出残渣を用い、この残渣からカテキン類を除去して酵素抽出を行うことで、従来にない香味豊かな茶抽出物が得られることを見出し、本発明を完成させた。
As a result of intensive studies to solve the above problems, the present inventors have conducted extraction using an enzyme (in this specification, sometimes referred to as “enzyme extraction”), and the amino acid concentration of the enzyme It has been thought that the action of increasing the catechins may not be sufficiently exhibited or inhibited by the presence of catechins. Based on this idea, when at least a part of catechins is removed from tea leaves and then enzymatic extraction of the tea leaves is performed, the amino acid content of the resulting tea extract is dramatically increased and the catechins content is reduced. I found out. The tea extract has an unprecedented composition, that is, the ratio of the total amount of amino acids to the tea leaf-derived solid content in the tea extract is 2.5% by weight or more (preferably 5.0% by weight or more). More preferably 7.0 wt% or more), and the ratio of the total amount of catechins is 15.0 wt% or less (preferably 13.5 wt% or less, more preferably 10.0 wt% or less, particularly preferably It was confirmed that the tea extract was usable as a flavor enhancer for tea beverages because it had umami and richness and no bitterness.
Further, as a result of further investigation, the present inventors have found that a fresh umami can be imparted when theanine is mixed with the tea extract at a certain ratio. And if you use a low temperature extract of tea leaves as this theanine, it becomes a tea extract with a fresh umami and thick body and reduced bitterness and astringency, especially using the extraction residue of the low temperature extract As a result, it was found that a tea extract with a rich flavor that has never been obtained can be obtained by removing catechins from the residue and performing enzyme extraction, thereby completing the present invention.

すなわち、本発明は下記の内容に関する。
1. 茶葉に溶媒を接触させて得られる茶抽出物であって、該茶抽出物中の茶葉由来固形分に対し、アミノ酸の総量の割合が2.5重量%以上(好ましくは5.0重量%以上、より好ましくは7.0重量%以上)であり、カテキン類の総量の割合が15.0重量%以下(好ましくは13.5重量%以下、より好ましくは10.0重量%以下、特に好ましくは8.0重量%以下)である、茶抽出物。
2. さらにテアニンを含有し、テアニンの割合がアミノ酸に対して0.1以上(好ましくは0.15以上)である、上記1に記載の茶抽出物。
3. テアニンが、茶葉を40℃以下の溶媒で抽出して得られる茶葉の低温抽出物として添加されたものである、上記2に記載の茶抽出物。
4. 茶葉の酵素抽出液を含む、上記1〜3のいずれか1項に記載の茶抽出物。
5. 酵素が、プロテアーゼ、セルラーゼ、ペクチナーゼから選択される1種以上である、上記4に記載の茶抽出物。
6. 酵素抽出液が、茶葉からカテキン類の少なくとも一部を除去し、この茶葉を酵素抽出して得られた酵素抽出液である、上記4または5に記載の茶抽出物。
7. 茶抽出物のBrixが、0.1〜20%である、上記1〜6のいずれか1項に記載の茶抽出物。
8. 茶抽出物が粉体状である、上記1〜6のいずれか1項に記載の茶抽出物。
9. 上記1〜8のいずれかに記載の茶抽出物を含有する、容器詰茶飲料。
10. 次の工程、
1.茶葉のカテキン類の少なくとも一部を除去する工程;及び
2.上記カテキンが除去された茶葉を酵素抽出して酵素抽出液を得る工程;
を含む、茶抽出物の製造方法。
11. カテキン類を除去する工程が、60℃以上の水性溶媒で抽出した高温抽出液の除去である、上記10に記載の茶抽出物の製造方法。
12. カテキン類を除去する工程が、酸処理による除去である、上記10に記載の茶抽出物の製造方法。
13. さらに、次の工程、
3.前記酵素抽出液にテアニンを混合してテアニン高含有茶抽出物を得る工程;
を含む、上記10〜12のいずれか1項に記載の茶抽出物の製造方法。
14. テアニンが、茶葉を40℃以下の溶媒で抽出して得られる茶葉の低温抽出物として添加されたものである、上記13に記載の茶抽出物の製造方法。
15. カテキン類を除去する茶葉が、前記低温抽出液を抽出した後の抽出残渣である、上記14に記載の茶抽出物の製造方法。
16. 茶葉の酵素抽出により得られる茶抽出物において、酵素抽出の前に茶葉に含まれるカテキン類の少なくとも一部を除去することにより、茶抽出物中のアミノ酸含量を高める方法。
That is, the present invention relates to the following contents.
1. A tea extract obtained by bringing a tea leaf into contact with a solvent, wherein the ratio of the total amount of amino acids to the tea leaf-derived solid content in the tea extract is 2.5% by weight or more (preferably 5.0% by weight or more) More preferably 7.0 wt% or more), and the ratio of the total amount of catechins is 15.0 wt% or less (preferably 13.5 wt% or less, more preferably 10.0 wt% or less, particularly preferably 8.0% by weight or less) tea extract.
2. The tea extract according to 1 above, further comprising theanine, wherein the proportion of theanine is 0.1 or more (preferably 0.15 or more ) based on the amino acid.
3. 3. The tea extract according to 2 above, wherein theanine is added as a low temperature extract of tea leaves obtained by extracting tea leaves with a solvent of 40 ° C. or lower.
4). The tea extract of any one of said 1-3 containing the enzyme extract of a tea leaf.
5. 5. The tea extract according to 4 above, wherein the enzyme is one or more selected from protease, cellulase, and pectinase.
6). 6. The tea extract according to 4 or 5 above, wherein the enzyme extract is an enzyme extract obtained by removing at least part of catechins from tea leaves and performing enzyme extraction on the tea leaves.
7. The tea extract according to any one of 1 to 6 above, wherein the Brix of the tea extract is 0.1 to 20%.
8). 7. The tea extract according to any one of 1 to 6 above, wherein the tea extract is in powder form.
9. A packaged tea beverage containing the tea extract according to any one of 1 to 8 above.
10. Next step,
1. 1. removing at least a portion of tea leaf catechins; Enzymatic extraction of tea leaves from which the catechin has been removed to obtain an enzyme extract;
A method for producing a tea extract, comprising:
11. 11. The method for producing a tea extract according to 10 above, wherein the step of removing catechins is removal of a high-temperature extract extracted with an aqueous solvent at 60 ° C. or higher.
12 11. The method for producing a tea extract as described in 10 above, wherein the step of removing catechins is removal by acid treatment.
13. Furthermore, the next step,
3. Mixing theanine into the enzyme extract to obtain a tea extract with a high content of theanine;
The manufacturing method of the tea extract of any one of said 10-12 containing this.
14 14. The method for producing a tea extract according to the above 13, wherein theanine is added as a low-temperature tea leaf extract obtained by extracting tea leaves with a solvent at 40 ° C. or lower.
15. 15. The method for producing a tea extract according to 14 above, wherein the tea leaf from which catechins are removed is an extraction residue after extracting the low-temperature extract.
16. A method for increasing the amino acid content in a tea extract by removing at least a part of catechins contained in tea leaves before the enzyme extraction in the tea extract obtained by enzyme extraction of tea leaves.

本発明の茶抽出物は、旨み・コク味成分であるアミノ酸を高濃度に含有し、苦味・渋味成分であるカテキン類が低減されているので、飲食品に添加して、風味の増強、旨みやコク味の付与を図ることができる。特に、本発明の茶抽出物を茶飲料に添加することにより、フレッシュな旨みと、厚みのあるコクを有する複雑な旨みとを備え、かつ苦渋みを抑制した容器詰茶飲料を提供することができる。   The tea extract of the present invention contains amino acids that are umami and richness components in high concentrations, and catechins that are bitterness and astringency components are reduced. Taste and richness can be imparted. In particular, by adding the tea extract of the present invention to a tea beverage, it is possible to provide a packaged tea beverage that has a fresh umami and a complex umami with a rich body and suppresses bitterness. it can.

発明の実施するための最良の形態BEST MODE FOR CARRYING OUT THE INVENTION

(茶抽出物)
本発明の茶抽出物は、旨味・コク味成分であるアミノ酸を高濃度に含有し、苦味・渋味成分であるカテキン類を低減させた茶抽出物である。本明細書でいう「茶抽出物」とは、茶葉に溶媒、特に水性溶媒を接触させて得られる茶葉の溶媒抽出物のことである。本発明の茶抽出物は、そのままで茶飲料として利用してもよいが、通常、茶飲料よりも濃く、すなわち可溶性固形分が多い抽出物(本明細書中、茶エキスとも表記する)として製造されるものであり、水又は茶飲料等の飲食物に添加して風味増強剤として用いられるものである。ここで、本発明の茶抽出物が液体の場合、そのBrixは、通常0.1〜20%程度である。本発明の茶抽出物は、上記液体状の茶抽出物を常法によりパウダー化して粉体状としてもよい。
本発明の茶抽出物(茶エキス)は、通常、茶葉の酵素抽出により得られる。本明細書でいう、酵素抽出とは、酵素を添加混合した茶葉を水性溶媒にて抽出すること又は酵素を添加した水性溶媒で茶葉の抽出を行うことを意味する。
本発明の茶抽出物は、上記したとおり、アミノ酸を高濃度に含有し、苦味・渋味成分が少ないことを特徴とするものである。具体的には、茶抽出物中、茶葉由来固形分に対してカテキン類の総量の割合が15.0重量%以下、好ましくは13.5重量%以下、より好ましくは10.0重量%以下、特に好ましくは8.0重量%以下であると、苦渋味を感じない。そして、このカテキン類含量の茶抽出物において、アミノ酸の総量の割合が、茶葉由来固形分に対して2.5重量%以上、好ましくは5.0重量%以上、より好ましくは7.0重量%以上であると、旨味・コク味を有する茶抽出物となる。本発明の茶抽出物は、従来の茶抽出物と比べ、アミノ酸含量が高いばかりか、カテキン類に対するアミノ酸の含量が高いため、飲料(特に茶飲料)に添加した場合に、苦渋味を与えずに旨味・コク味のみを増強することができる。
(Tea extract)
The tea extract of the present invention is a tea extract containing a high concentration of amino acids that are umami and rich taste components and reduced catechins that are bitter and astringent components. The term “tea extract” as used herein refers to a solvent extract of tea leaves obtained by bringing tea leaves into contact with a solvent, particularly an aqueous solvent. The tea extract of the present invention may be used as it is as a tea beverage, but is usually produced as an extract that is thicker than a tea beverage, that is, has a higher soluble solid content (also referred to herein as a tea extract). It is used as a flavor enhancer by being added to food or drink such as water or tea beverage. Here, when the tea extract of the present invention is liquid, its Brix is usually about 0.1 to 20%. The tea extract of the present invention may be made into a powder form by pulverizing the liquid tea extract by a conventional method.
The tea extract (tea extract) of the present invention is usually obtained by enzymatic extraction of tea leaves. As used herein, enzyme extraction means extraction of tea leaves to which an enzyme has been added and mixed with an aqueous solvent or extraction of tea leaves with an aqueous solvent to which an enzyme has been added.
As described above, the tea extract of the present invention is characterized by containing an amino acid at a high concentration and having few bitterness and astringency components. Specifically, in the tea extract, the ratio of the total amount of catechins to the tea leaf-derived solid content is 15.0 wt% or less, preferably 13.5 wt% or less, more preferably 10.0 wt% or less, Particularly preferably, the bitter and astringent taste is not felt when the content is 8.0% by weight or less. In this tea extract having a catechin content, the ratio of the total amount of amino acids is 2.5% by weight or more, preferably 5.0% by weight or more, more preferably 7.0% by weight, based on the solid content derived from tea leaves. When it is above, it becomes a tea extract having umami and richness. The tea extract of the present invention not only has a high amino acid content, but also has a high amino acid content with respect to catechins, so that it does not give bitter astringency when added to beverages (especially tea beverages). Only umami and richness can be enhanced.

さらに、本発明の茶抽出物にテアニンを一定量の割合で混合したテアニン高含有茶抽出物は、旨味・コク味に加えてフレッシュな旨味をも増強できる。テアニンの含量は、茶抽出物中のアミノ酸のうち、テアニンの割合が0.1以上、好ましくは0.15となるように添加するのが好ましい。または、テアニン高含有茶抽出物中の茶葉由来固形分に対し、テアニンの割合が0.3重量%以上、好ましくは0.6重量%以上、より好ましくは0.8重量%以上、さらにより好ましくは1.0重量%以上、特に好ましくは1.5重量%以上となるように、テアニンを添加するのが好ましい。テアニンは、茶葉より精製されたものとして市販されているもの等を用いてもよいが、茶葉の低温抽出物として添加すると、ヘキサナール等の香気成分も混合されるので、よりフレッシュな旨味と厚みのあるコク味とを付与することができる。ここで、茶葉の低温抽出物とは、茶葉を40℃以下の水性溶媒で抽出して得られるものをいい、緑茶葉を40℃以下の水で浸漬、濾過して得られる緑茶抽出物(低温抽出液)を例示することができる。
上記のとおり、本発明の茶抽出物は、茶飲料、菓子等の飲食品原料として用いることができる。本発明の茶抽出物は、従来の茶抽出物にない、フレッシュな風味とコク・厚みのある旨味を有し苦味・渋味の少ないものであるから、茶飲料として好適に提供される。
本発明の茶抽出物は、そのままで、または必要に応じて適宜希釈等を行って茶飲料とすることができる。この茶飲料を容器に充填すると、急須で入れた高級茶のような豊かなコク・旨味を有し、苦味・渋味の少ない茶飲料として、日常的に摂取できるものとなる。ここでいう容器とは、特に限定されるものではなく、例えばペットボトル、缶、瓶、紙パック等の容器が挙げられる。
茶飲料のpHは、5.9〜6.3程度に調整すると、本発明の特徴とする香味を長期間に渡り保持でき、さらに褐変防止にも有利である。また、酵素抽出液の調製する際にプロテアーゼを用いた場合には、保存安定性(沈殿防止)に優れた茶飲料とすることができる。
Furthermore, the theanine-rich tea extract in which theanine is mixed with the tea extract of the present invention in a certain ratio can enhance the fresh umami in addition to the umami and richness. The theanine content is preferably added so that the theanine content of the amino acids in the tea extract is 0.1 or more , preferably 0.15 . Or, the proportion of theanine is 0.3% by weight or more, preferably 0.6% by weight or more, more preferably 0.8% by weight or more, and still more preferably, based on the tea leaf-derived solid content in the tea extract with a high content of theanine Is preferably 1.0% by weight or more, particularly preferably 1.5% by weight or more. Theanine may be commercially available as purified from tea leaves, but when added as a low temperature extract of tea leaves, aroma components such as hexanal are also mixed, so fresher umami and thickness A certain richness can be imparted. Here, the low temperature extract of tea leaves refers to those obtained by extracting tea leaves with an aqueous solvent at 40 ° C. or lower, and green tea extracts (low temperature) obtained by immersing and filtering green tea leaves with water at 40 ° C. or lower. Extract)).
As above-mentioned, the tea extract of this invention can be used as food-drinks raw materials, such as a tea drink and confectionery. The tea extract of the present invention has a fresh flavor, richness, and thick umami, which is not found in conventional tea extracts, and is less prone to bitterness and astringency, and thus is suitably provided as a tea beverage.
The tea extract of the present invention can be made into a tea beverage as it is or by appropriately performing dilution or the like as necessary. When this tea beverage is filled in a container, it can be ingested on a daily basis as a tea beverage having rich richness and umami like a high-quality tea put in a teapot and less bitterness and astringency. A container here is not specifically limited, For example, containers, such as a plastic bottle, a can, a bottle, a paper pack, are mentioned.
When the pH of the tea beverage is adjusted to about 5.9 to 6.3, the flavor characteristic of the present invention can be maintained over a long period of time, and it is advantageous for preventing browning. Moreover, when protease is used when preparing an enzyme extract, a tea beverage excellent in storage stability (precipitation prevention) can be obtained.

(茶抽出物の製造方法)
本発明のアミノ酸を高濃度に含有しカテキン類が除去された茶抽出物の製造方法は、上記の特定範囲のアミノ酸及びカテキン類を含有しうる方法であれば、特に制限されない。例えば、ア)アミノ酸が高濃度に抽出される茶葉の低温抽出液から、公知の方法(例えば樹脂吸着)によりカテキン類を除去する方法、イ)緑茶葉に5〜50%、好ましくは10〜30%程度の塩酸を加え、高温(約80℃)で浸漬することにより、茶葉中のタンパク質を加水分解してアミノ酸を生成させるとともに、カテキン類を沈殿除去させることにより、アミノ酸を高濃度に含有し、カテキン類が低減された茶抽出物を得る方法(酸処理法)等が挙げられる。しかし、ア)の方法では効率が悪く、イ)の酸処理法で得られる茶抽出物は、多量の酸が含まれるため中和剤の添加が必要であり、その結果、多量の塩が生成されるために香味的に好ましくないという問題がある。本発明者らは、上記本発明の茶抽出物を得る方法として、茶葉からカテキン類の少なくとも一部を除去した後、この茶葉を酵素抽出することにより、本発明のアミノ酸を高濃度に含有しカテキン類が除去された茶抽出物(酵素抽出液)で、塩などの本来茶葉に含まれていない成分を含有しない香味的に優れた茶抽出物を、簡便に得ることができることを見出した。この製造方法では、茶葉からカテキン類の少なくとも一部を除去することで、この茶葉を酵素処理する際に、酵素の作用を高めることができ、その結果、よりアミノ酸を高濃度に含有しカテキン類を低減させることができると考えられる。
また、本発明者らは、上記の酵素抽出液と別途調製したテアニン、特に茶葉の低温抽出液とを混合することにより、コク・厚みのある旨味を有し、苦味・渋味が少なく、かつ、フレッシュな旨味を有する茶抽出物が得られることも見出している。
本発明においては、茶葉からカテキン類を除去する工程、この茶葉から酵素抽出液を得る工程、および必要に応じて低温抽出液を得る工程を、同一抽出機内で連続的に行うことができるが、各行程についてその詳細を以下に説明する。
(Method for producing tea extract)
The method for producing a tea extract containing the amino acid of the present invention in a high concentration and from which catechins have been removed is not particularly limited as long as it is a method that can contain the above-mentioned specific range of amino acids and catechins. For example, a) a method of removing catechins by a known method (for example, resin adsorption) from a low-temperature tea leaf extract from which amino acids are extracted at a high concentration, and b) a green tea leaf of 5 to 50%, preferably 10 to 30 By adding about 1% hydrochloric acid and soaking at high temperature (about 80 ° C), the protein in tea leaves is hydrolyzed to produce amino acids, and catechins are precipitated and removed, so that amino acids are contained in high concentration. And a method (acid treatment method) for obtaining a tea extract with reduced catechins. However, the method (a) is inefficient, and the tea extract obtained by the acid treatment method (a) contains a large amount of acid, so it is necessary to add a neutralizing agent. As a result, a large amount of salt is produced. Therefore, there is a problem that the flavor is not preferable. As a method for obtaining the tea extract of the present invention, the present inventors have removed at least a part of catechins from tea leaves, and then enzymatically extracted the tea leaves, thereby containing the amino acid of the present invention at a high concentration. It has been found that a tea extract (enzyme extract) from which catechins have been removed can be easily obtained with a flavorful tea extract that does not contain components such as salt that are not originally contained in tea leaves. In this production method, by removing at least a part of the catechins from the tea leaves, the enzyme action can be enhanced when the tea leaves are treated with an enzyme. As a result, the catechins contain a higher concentration of amino acids. Can be reduced.
In addition, the present inventors mixed the above-described enzyme extract with separately prepared theanine, particularly a low-temperature extract of tea leaves, so that it has a rich and thick umami taste, less bitterness and astringency, and It has also been found that a tea extract having a fresh umami taste can be obtained.
In the present invention, the step of removing catechins from tea leaves, the step of obtaining an enzyme extract from the tea leaves, and the step of obtaining a low temperature extract as necessary can be carried out continuously in the same extractor, Details of each process will be described below.

(第1工程:カテキン類を除去する工程)
上記したとおり、本発明の茶抽出物の製造方法では、まず茶葉からカテキン類を除去することを特徴とする。ここで、本明細書におけるカテキン類とは、カテキン、エピカテキン、ガロカテキン、エピガロカテキン、カテキンガレート、エピカテキンガレート、ガロカテキンガレートおよびエピガロカテキンガレートの総称を表す。
茶葉からカテキン類を除去する方法は、カテキン類の少なくとも一部を除去しうる方法であれば何ら制限されるものではなく、例えば、茶葉に水性溶媒を接触させて茶葉抽出液を得、この抽出液を除去(廃棄)する方法を例示できる。特に、カテキン類は高温で抽出されやすいという性質があるから、茶葉に高温(好ましくは60℃以上)の溶媒(好ましくは水)を接触させて高温抽出液を得、この抽出液を除去(廃棄)する方法が好適である。
また、効率よくカテキン類のみを除去する方法として、吸着樹脂を用いる方法、例えば、WO2005/077384号公報に記載の高温(好ましくは60℃以上)で吸着樹脂と接触させる方法等が挙げられる。この抽出液は、選択的にカテキン類が除去されており、旨味成分等の茶由来の成分を含んでいるので、次の酵素抽出の工程の抽出溶媒として利用することができる。その他、公知の酸やアルカリ溶液、有機溶媒を用いる方法によっても茶葉中のカテキン類を選択的に除去することが可能である。具体的には、茶葉に0.05〜5%、好ましくは0.1〜2%程度の塩酸(酸溶液)を添加(pH1〜4程度)して浸漬し、高温(約80℃)で保持してカテキン類を沈殿除去させて酸処理溶液を得る方法が例示される。
作業性の観点から、また茶葉本来の成分をそのまま維持できるという風味の観点からは、高温抽出液を得てこれを除去する方法がよい。
上記の高温抽出液を得る際の溶媒は、水性溶媒であればよく、蒸留水、イオン交換水、含水アルコール等を用いることができるが、アルコールの沸点を考慮すると蒸留水やイオン交換水を用いるのが好ましい。
(First step: step of removing catechins)
As described above, the method for producing a tea extract of the present invention is characterized in that catechins are first removed from tea leaves. Here, the catechins in the present specification represent a generic name of catechin, epicatechin, gallocatechin, epigallocatechin, catechin gallate, epicatechin gallate, gallocatechin gallate and epigallocatechin gallate.
The method for removing catechins from tea leaves is not limited as long as it is a method that can remove at least a part of catechins. For example, a tea leaf extract is obtained by contacting tea leaves with an aqueous solvent, and this extraction is performed. A method for removing (disposing) the liquid can be exemplified. In particular, since catechins are easily extracted at high temperature, a high temperature (preferably 60 ° C or higher) solvent (preferably water) is brought into contact with tea leaves to obtain a high temperature extract, and this extract is removed (discarded) ) Is preferred.
Moreover, as a method for efficiently removing only catechins, a method using an adsorbent resin, for example, a method of contacting the adsorbent resin at a high temperature (preferably 60 ° C. or higher) described in WO2005 / 077384, and the like can be mentioned. Since this extract has catechins selectively removed and contains tea-derived components such as umami components, it can be used as an extraction solvent in the subsequent enzyme extraction step. In addition, catechins in tea leaves can be selectively removed by a method using a known acid, alkali solution, or organic solvent. Specifically, 0.05 to 5%, preferably about 0.1 to 2% hydrochloric acid (acid solution) is added to the tea leaves (pH of about 1 to 4) and immersed at a high temperature (about 80 ° C.). Then, a method for obtaining an acid treatment solution by precipitation removal of catechins is exemplified.
From the viewpoint of workability and from the viewpoint of flavor that the original components of tea leaves can be maintained as they are, a method of obtaining a high-temperature extract and removing it is preferable.
The solvent for obtaining the high-temperature extract may be an aqueous solvent, and distilled water, ion-exchanged water, hydrous alcohol or the like can be used, but distilled water or ion-exchanged water is used in consideration of the boiling point of the alcohol. Is preferred.

茶葉からカテキン類の少なくとも一部が除去されたかどうかの判断は、カテキン類を除去する工程、例えば上記の高温抽出液や酸処理溶液のカテキン類濃度を測定することで、茶葉からカテキン類が抽出除去されたかどうかを評価することができる。
カテキン類は、公知の方法(例えば、フィルター(0.45μm)で濾過した液を高速液体クロマトグラム(HPLC)による分離分析する方法)により定量することができる。
なお、原料となる茶葉には、煎茶、番茶、ほうじ茶、玉露、かぶせ茶、甜茶等の蒸し製の不発酵茶(緑茶);嬉野茶、青柳茶、各種中国茶等の釜炒茶等の不発酵茶;包種茶、鉄観音茶、ウーロン茶等の半発酵茶;紅茶、阿波番茶、プアール茶などの発酵茶等、いずれのものも用いることができる。なかでも、特に旨味やコク味が重要視される不発酵茶(緑茶)および半発酵茶が好適に用いられる。
さらに、この原料となる茶葉としては、新しい茶葉を用いることもできるが、経済性等を考慮すれば、後述するように低温抽出液を抽出した後の抽出残渣を用いることが好ましい。本発明のカテキン類を除去する工程において、カテキン類だけでなくアミノ酸も除去される可能性があるためである。予め抽出されやすいアミノ酸を確保しておくことが、アミノ酸収率の観点から好ましい。
Whether or not at least part of the catechins has been removed from the tea leaves is determined by the step of removing the catechins, for example, by measuring the concentration of the catechins in the above high-temperature extract or acid treatment solution, It can be evaluated whether it has been removed or not.
Catechins can be quantified by a known method (for example, a method of separating and analyzing a liquid filtered with a filter (0.45 μm) by high performance liquid chromatogram (HPLC)).
In addition, the tea leaves used as ingredients are steamed non-fermented tea (green tea) such as sencha, bancha, hojicha, gyokuro, kabusecha, and strawberry tea; Fermented teas: Semi-fermented teas such as baked tea, iron kannon tea and oolong tea; fermented teas such as black tea, Awaban tea and Puer tea can be used. Of these, non-fermented tea (green tea) and semi-fermented tea, which are particularly important for umami and rich taste, are preferably used.
Further, as the tea leaves used as the raw material, new tea leaves can be used. However, in view of economy and the like, it is preferable to use an extraction residue after extracting the low temperature extract as described later. This is because not only catechins but also amino acids may be removed in the step of removing catechins of the present invention. It is preferable from the viewpoint of amino acid yield to secure an amino acid that is easily extracted in advance.

後述するが、本発明者らの検討によると、緑茶葉を低温抽出すると、その抽出液中には固形分あたりのカテキン類が15〜25重量%程度含まれており、アミノ酸が1.0〜7.0重量%(うちテアニンが0.4〜3.5重量%)含まれていた。アミノ酸中のテアニンの割合は、0.4〜0.5程度であった(比較例A1、A1’、実施例D1、D1’、E1参照)。また、緑茶葉を高温抽出すると、その抽出液中には固形分あたりのカテキン類が15重量%程度含まれており、アミノ酸が2.5重量%(うちテアニンが1.5重量%)含まれていた。アミノ酸中のテアニンの割合は、0.5程度であった(実施例B1参照)。さらに、緑茶葉を低温抽出した抽出残渣に高温抽出を施すと、その抽出液中には、固形分あたりのカテキン類が30〜35重量%程度含まれており、アミノ酸が0.4〜2.0重量%(うちテアニンが0〜1.5重量%)含まれていた。アミノ酸中のテアニンの割合は、0〜0.6程度であった(実施例D2、D2’、E2参照)。さらにまた、酸処理によるカテキン除去では、その酸処理溶液中には固形分あたりのカテキン類が10重量%程度含まれており、アミノ酸が3.5重量%程度(うちテアニンが1.5重量%)含まれていた。アミノ酸中のテアニンの割合は、0.4程度であった(実施例C1参照)。
この結果から、カテキン類を効率的にかつ簡便に除去するのは、緑茶葉を低温抽出した抽出残渣を高温抽出して、この高温抽出液を除去(廃棄)する方法であることがわかる。また、緑茶葉の低温抽出液中には、アミノ酸、特にテアニンが多く含まれることから、この低温抽出液を後述の酵素抽出液に添加するテアニンとして利用するのが良いこともわかる。
As will be described later, according to the study by the present inventors, when green tea leaves are extracted at a low temperature, the extract contains about 15 to 25% by weight of catechins per solid content, and amino acids are 1.0 to 7.0% by weight (of which 0.4 to 3.5% by weight of theanine) was contained. The ratio of theanine in the amino acid was about 0.4 to 0.5 (see Comparative Examples A1, A1 ′, Examples D1, D1 ′, E1). When green tea leaves are extracted at a high temperature, the extract contains about 15% by weight of catechins per solid content and 2.5% by weight of amino acids (of which theanine is 1.5% by weight). It was. The ratio of theanine in the amino acid was about 0.5 (see Example B1). Furthermore, when high temperature extraction is performed on the extraction residue obtained by low temperature extraction of green tea leaves, the extract contains about 30 to 35% by weight of catechins per solid content, and amino acids of 0.4 to 2. 0% by weight (of which 0 to 1.5% by weight of theanine) was contained. The ratio of theanine in the amino acid was about 0 to 0.6 (see Examples D2, D2 ′, E2). Furthermore, in catechin removal by acid treatment, the acid treatment solution contains about 10% by weight of catechins per solid content, about 3.5% by weight of amino acids (of which theanine is 1.5% by weight) ) Was included. The ratio of theanine in the amino acid was about 0.4 (see Example C1).
From this result, it can be seen that efficient and simple removal of catechins is a method of extracting (discarding) this high-temperature extract by high-temperature extraction of the extraction residue obtained by low-temperature extraction of green tea leaves. Moreover, since the low temperature extract of green tea leaves contains a large amount of amino acids, particularly theanine, it can be seen that this low temperature extract can be used as theanine added to the enzyme extract described later.

(第2工程:酵素抽出液を得る工程)
本発明では、第1工程でカテキン類が除去された茶葉に酵素抽出を行う。本明細書における酵素抽出とは、酵素を添加混合した茶葉を水性溶媒にて抽出すること又は酵素を添加した水性溶媒で茶葉の抽出を行うことを意味する。
ここで使用される酵素は、抽出液中のアミノ酸を増加させることができる酵素であればよく、例えばプロテアーゼ、α−アミラーゼ、セルラーゼ、ヘミセルラーゼ、ペクチナーゼ、プロトペクチナーゼ等を1種又は複数種類併用して用いることができる。なかでも、茶葉中の不溶性タンパク質を分解して低分子ペプチド、アミノ酸に可溶化しうるプロテアーゼと、茶葉中の繊維質を分解して茶葉中に存在するタンパク質を遊離させてアミノ酸の抽出効率を高めるセルラーゼ又はペクチナーゼ等との併用が、アミノ酸の抽出効率の観点から好適である。
上記のセルラーゼとは、セルロースのβ−1,4−グリコシド結合を加水分解してセルビオースを生成する反応を行う酵素である。食品で利用可能なセルラーゼであればその由来や、精製度等に限定されることなく用いることができる。市販されているセルラーゼとしては、セルロシンT2、AC40、AL(阪急共栄物産株式会社)、セルラーゼ「オノズカ」3S(ヤクルト薬品工業株式会社)、セルラーゼT「アマノ」4、A「アマノ」3(天野エンザイム株式会社)等が例示できる。
(Second step: step of obtaining an enzyme extract)
In the present invention, enzyme extraction is performed on tea leaves from which catechins have been removed in the first step. Enzyme extraction in the present specification means extraction of tea leaves mixed with an enzyme with an aqueous solvent, or extraction of tea leaves with an aqueous solvent added with an enzyme.
The enzyme used here may be any enzyme that can increase the amino acids in the extract. For example, one or more kinds of protease, α-amylase, cellulase, hemicellulase, pectinase, protopectinase, etc. may be used in combination. Can be used. Among them, proteases that can dissolve insoluble proteins in tea leaves to solubilize low-molecular peptides and amino acids, and fibers in tea leaves to release proteins present in tea leaves to increase amino acid extraction efficiency. Use in combination with cellulase or pectinase is preferable from the viewpoint of amino acid extraction efficiency.
The above cellulase is an enzyme that performs a reaction of hydrolyzing the β-1,4-glycosidic bond of cellulose to produce cellobiose. Any cellulase that can be used in foods can be used without being limited by its origin, degree of purification, and the like. Commercially available cellulases include cellulosin T2, AC40, AL (Hankyu Kyoei Bussan Co., Ltd.), cellulase “Onozuka” 3S (Yakult Pharmaceutical Co., Ltd.), cellulase T “Amano” 4, A “Amano” 3 (Amano Enzyme) Etc.).

上記のペクチナーゼ(ペクチンデポリメラーゼ又はポリガラクトウロニダーゼとも称される)とは、ポリガラクツロン酸(ペクチン酸)のα−1,4’−グリコシド結合を加水分解する反応を行う酵素である。食品で利用可能なペクチナーゼであればその由来や、精製度等に限定されることなく用いることができ、果汁の清澄化、搾汁の歩留まり向上等の利用を目的として市販されているペクチナーゼ等を用いることができる。このようなペクチナーゼとしては、セルロシンPC5、PE60、PEL(阪急共栄物産株式会社)、ペクチナーゼ3S、HL(ヤクルト薬品工業株式会社)、ペクチナーゼ「アマノ」PL、G「アマノ」(天野エンザイム株式会社)等が例示できる。
上記のプロテアーゼとは、タンパク質、ペプチドに作用してペプチド結合の加水分解を触媒する酵素である。プロテアーゼは、タンパク質、ペプチドに作用して低分子ペプチドを生成するエンドペプチダーゼ(プロテイナーゼ)と、ペプチドに作用してアミノ酸を生成するエキソペプチダーゼ(ペプチダーゼ)の2種類に大別される。これらいずれのプロテアーゼを用いてもよいが、特にアミノ酸を生成しうるエキソペプチダーゼが好適である。このようなプロテアーゼは食品で利用可能なものであればその由来や、精製度等に限定されることなく用いることができ、作用至適pH等を考慮して選択すればよい。市販されているプロテアーゼとしては、オリエンターゼ22BF、90N、ONS、20A、ヌクレイシン、(阪急共栄物産株式会社)、パンチダーゼNP−2、パパインソルブル、プロテアーゼYP−SS(ヤクルト薬品工業株式会社)、デナチームAP、デナプシン、食品用精製パパイン(ナガセケムテック株式会社)、プロテアーゼM「アマノ」、A「アマノ」G、P「アマノ」3G、N「アマノ」、グルタミナーゼF「アマノ」100、ニューラーゼF、パンクレアチンF、パパインW−40、プロメラインF(天野エンザイム株式会社)等が例示できる。
The pectinase (also referred to as pectin depolymerase or polygalacturonidase) is an enzyme that performs a reaction to hydrolyze the α-1,4′-glycoside bond of polygalacturonic acid (pectinic acid). Any pectinase that can be used in foods can be used without limitation on its origin, degree of purification, etc., and pectinase that is commercially available for the purpose of clarifying fruit juice, improving the yield of juice, etc. Can be used. Such pectinases include cellulosin PC5, PE60, PEL (Hankyu Kyoei Bussan Co., Ltd.), pectinase 3S, HL (Yakult Pharmaceutical Co., Ltd.), pectinase “Amano” PL, G “Amano” (Amano Enzyme Co., Ltd.), etc. Can be illustrated.
The above protease is an enzyme that acts on proteins and peptides to catalyze the hydrolysis of peptide bonds. Proteases are roughly classified into two types: endopeptidases (proteinases) that act on proteins and peptides to produce low molecular weight peptides, and exopeptidases (peptidases) that act on peptides to produce amino acids. Any of these proteases may be used, but exopeptidase capable of producing an amino acid is particularly preferable. As long as such protease can be used in foods, it can be used without limitation on its origin, purification degree, etc., and may be selected in consideration of optimum pH of action and the like. Commercially available proteases include orientase 22BF, 90N, ONS, 20A, Nucleicin (Hankyu Kyoei Bussan Co., Ltd.), Pandidase NP-2, Papain Soluble, Protease YP-SS (Yakult Pharmaceutical Co., Ltd.), Denateam AP, Denapsin, Purified Papain for Food (Nagase Chemtech Co., Ltd.), Protease M “Amano”, A “Amano” G, P “Amano” 3G, N “Amano”, Glutaminase F “Amano” 100, Neurase F, Examples include pancreatin F, papain W-40, and promeline F (Amano Enzyme Co., Ltd.).

酵素抽出の条件は、用いる酵素の種類や茶葉の種類、所望される嗜好性等により異なるが、通常、その配合量は茶葉に対して、重量を基準にして、0.0001〜0.1、好ましくは0.001〜0.05重量部程度である。0.0001重量部未満であると、抽出液中のアミノ酸を増加させるのに十分な効果が得られない。また、0.1重量部より多く配合してもアミノ酸の抽出効率のさらなる向上が期待できないので経済的に不利であり、また酵素の種類によってはその呈味が抽出物に影響を及ぼすことがある。
酵素抽出の温度は、用いる酵素の至適条件を鑑みて適宜選択すればよいが、通常、20〜50℃、好ましくは35〜45℃程度である。20℃より低温では抽出効率が悪く、50℃より高温で酵素抽出を行うと抽出液に異味が生じる場合がある。
酵素抽出の時間も適宜選択すればよいが、通常、0.5〜20時間、好ましくは5〜18時間程度である。0.5時間より短いと酵素反応が十分に行われないことがある。また、20時間以上行ってもアミノ酸の抽出効率のさらなる向上が期待できないので経済的に不利であり、また酵素の種類によってはその呈味が抽出物に影響を及ぼすことがある。
なお、酵素抽出時のpHは、用いる酵素の至適pHを鑑みて設定するのがよく、必要に応じて、pH調整剤を添加することができる。
酵素反応(酵素抽出)は、攪拌下または循環通液により行うのが好ましい。
The conditions for enzyme extraction vary depending on the type of enzyme used, the type of tea leaf, the desired palatability, etc., but usually the blending amount is 0.0001 to 0.1 based on the weight of the tea leaf, Preferably it is about 0.001-0.05 weight part. If the amount is less than 0.0001 parts by weight, an effect sufficient to increase amino acids in the extract cannot be obtained. Moreover, even if it mixes more than 0.1 weight part, since the further improvement of the extraction efficiency of an amino acid cannot be expected, it is economically disadvantageous, and the taste may affect an extract depending on the kind of enzyme. .
The temperature of the enzyme extraction may be appropriately selected in view of the optimum conditions for the enzyme to be used, but is usually about 20 to 50 ° C, preferably about 35 to 45 ° C. When the temperature is lower than 20 ° C., the extraction efficiency is poor, and when the enzyme is extracted at a temperature higher than 50 ° C., the extract may have a different taste.
The enzyme extraction time may be appropriately selected, but is usually 0.5 to 20 hours, preferably about 5 to 18 hours. If the time is shorter than 0.5 hour, the enzyme reaction may not be sufficiently performed. Moreover, since further improvement in the extraction efficiency of amino acids cannot be expected even after 20 hours or more, it is economically disadvantageous, and depending on the type of enzyme, the taste may affect the extract.
In addition, it is good to set pH at the time of enzyme extraction in view of the optimal pH of the enzyme to be used, and a pH adjuster can be added as needed.
The enzyme reaction (enzyme extraction) is preferably carried out under stirring or by circulation.

酵素反応後、約60〜121℃で2秒〜20分間程度加熱することにより、酵素を失活させる。その後、茶抽出物(酵素抽出液)の風味劣化を防ぐため、直ちに冷却するのが好ましい。得られた茶抽出物は、必要に応じて、遠心分離、濾過等の分離操作を行って、清澄度を高めることもできる。また、濃縮操作を行って濃縮液の形態とすることもできる。さらに、乾燥操作を行って乾燥物の形態(粉末形態)とすることもできる。
このようにして得られる茶抽出物(酵素抽出液)は、高濃度のアミノ酸と低濃度のカテキン類を含有する。後述するが、本発明者らの検討によると、緑茶葉を低温抽出してカテキン類の一部を除去した抽出残渣(茶葉)を用いて酵素抽出を行った場合、その酵素抽出液中には固形分あたりのアミノ酸が4.0〜6.0重量%程度(うちテアニンが0.05〜0.3重量%)含まれており、カテキン類が7.0〜8.5重量%程度含まれていた。アミノ酸(a)とカテキン類(b)との比率(a/b)を算出すると、0.6〜0.7であった(比較例A2、A2’参照)。また、緑茶葉を高温抽出してカテキン類の一部を除去した抽出残渣(茶葉)を用いて酵素抽出を行った場合、その酵素抽出液中には固形分あたりのアミノ酸が11重量%程度(うちテアニンが0.2重量%)含まれており、カテキン類が0.7重量%含まれていた。アミノ酸(a)とカテキン類(b)との比率(a/b)を算出すると、15.8であった(実施例B2参照)。さらに、緑茶葉を低温抽出した抽出残渣に高温抽出を施したその抽出残渣(茶葉)に酵素抽出を行った場合、その酵素抽出液中には、固形分あたりのアミノ酸が7.5〜11.5重量%程度(うちテアニンが0.03〜0.7重量%)含まれており、カテキン類が0.5〜6.0重量%含まれていた。アミノ酸(a)とカテキン類(b)との比率(a/b)を算出すると、1.0〜16.0であった(実施例D3、D3’、E3参照)。さらにまた、酸処理によるカテキン除去を行った茶葉に酵素抽出を行った場合、その酵素抽出液中には固形分あたりのアミノ酸が12.5重量%程度(うちテアニンが0.3重量%)含まれており、カテキン類が8.0重量%程度含まれていた。アミノ酸(a)とカテキン類(b)との比率(a/b)を算出すると、1.6であった(実施例C2参照)。
After the enzyme reaction, the enzyme is inactivated by heating at about 60 to 121 ° C. for about 2 seconds to 20 minutes. Then, in order to prevent the flavor deterioration of a tea extract (enzyme extract), it is preferable to cool immediately. The obtained tea extract may be subjected to a separation operation such as centrifugation or filtration, if necessary, to increase the clarity. Moreover, it can also be made into the form of a concentrate by performing concentration operation. Furthermore, a drying operation can be performed to obtain a dry product form (powder form).
The tea extract (enzyme extract) thus obtained contains a high concentration of amino acids and a low concentration of catechins. As will be described later, according to the study by the present inventors, when enzyme extraction was performed using an extraction residue (tea leaf) obtained by removing green tea leaves at a low temperature to remove a part of catechins, Contains about 4.0 to 6.0% by weight of amino acid per solid content (including 0.05 to 0.3% by weight of theanine), and contains about 7.0 to 8.5% by weight of catechins. It was. The ratio (a / b) between the amino acid (a) and the catechins (b) was calculated to be 0.6 to 0.7 (see Comparative Examples A2 and A2 ′). In addition, when enzyme extraction is performed using an extraction residue (tea leaf) obtained by extracting green tea leaves at a high temperature to remove a part of catechins, the enzyme extract contains about 11% by weight of amino acids per solid content ( Of these, 0.2% by weight of theanine was contained, and 0.7% by weight of catechins were contained. The ratio (a / b) between the amino acid (a) and the catechins (b) was calculated to be 15.8 (see Example B2). Furthermore, when enzyme extraction is performed on an extraction residue (tea leaf) obtained by subjecting an extraction residue obtained by low-temperature extraction of green tea leaves to high-temperature extraction, the amino acid per solid content is 7.5 to 11. About 5% by weight (of which 0.03 to 0.7% by weight of theanine) was contained, and 0.5 to 6.0% by weight of catechins was contained. The ratio (a / b) between the amino acid (a) and the catechins (b) was calculated to be 1.0 to 16.0 (see Examples D3, D3 ′, and E3). Furthermore, when enzyme extraction is performed on tea leaves that have been subjected to catechin removal by acid treatment, the enzyme extract contains about 12.5% by weight of amino acids per solid (of which theanine is 0.3% by weight). It contained about 8.0% by weight of catechins. The ratio (a / b) between the amino acid (a) and the catechins (b) was calculated to be 1.6 (see Example C2).

この結果から、緑茶葉を高温抽出してカテキン類を除去した後または酸処理によるカテキン類を除去した後に、酵素抽出することにより、高濃度のアミノ酸と低濃度のカテキン類を含有する酵素抽出液が得られることがわかる。第1工程の結果と合わせると、カテキン類が効率的に除去された茶葉を用いて酵素抽出を行うことによって、よりアミノ酸を高濃度に含有し、カテキン類を低濃度に含有する茶抽出物(酵素抽出液)が得られることがわかる。これは、茶葉中のカテキン類を除去することによって、酵素の反応が高められ、酵素の作用が十分発揮されたためと考えられる。
なお、第2工程で得られる酵素抽出液中のアミノ酸含量、カテキン含量は、所望する茶抽出物の仕様により適宜設定すればよいが、通常、固形分あたりのアミノ酸の総量の割合が2.5重量%、好ましくは7.0重量%以上となるようにすると、旨味・コク味を有する茶抽出物となる。また、固形分あたりのカテキン類の総量の割合が15.0重量%以下、好ましくは10.0重量%以下となるようにすると、苦渋味がほとんど感じられない。この酵素抽出液中のアミノ酸(a)とカテキン類(b)との比率(a/b)が1以上、好ましくは5以上、より好ましくは10以上、特に好ましくは15以上となる茶抽出物(酵素抽出液)は、コク・厚みのある豊かな旨味を有し苦味や渋味がほとんどなく、茶飲料等の風味増強剤として有用であることを確認している。
From this result, after extracting green tea leaves at high temperature and removing catechins or after removing catechins by acid treatment, an enzyme extract containing high-concentration amino acids and low-concentration catechins by enzyme extraction It can be seen that Combined with the result of the first step, by performing enzyme extraction using tea leaves from which catechins have been efficiently removed, a tea extract containing a higher concentration of amino acids and a lower concentration of catechins ( It can be seen that an enzyme extract) is obtained. This is thought to be because the reaction of the enzyme was enhanced by removing the catechins in the tea leaves, and the action of the enzyme was sufficiently exerted.
The amino acid content and catechin content in the enzyme extract obtained in the second step may be appropriately set according to the specifications of the desired tea extract, but usually the ratio of the total amount of amino acids per solid content is 2.5. When it is adjusted to be at least 7% by weight, preferably a tea extract having umami and richness. Further, when the ratio of the total amount of catechins per solid content is 15.0% by weight or less, preferably 10.0% by weight or less, bitterness and astringency are hardly felt. A tea extract in which the ratio (a / b) of amino acid (a) to catechins (b) in this enzyme extract is 1 or more, preferably 5 or more, more preferably 10 or more, and particularly preferably 15 or more. The enzyme extract) has been confirmed to be useful as a flavor enhancer for tea beverages and the like with a rich and rich umami taste and little bitterness or astringency.

(第3工程:テアニン高含有茶抽出物を得る工程)
本発明は、上記の酵素抽出により得られる茶抽出物(酵素抽出液)にテアニンを混合することにより、コク・厚みのある豊かな旨味に加えて、フレッシュな旨味をも増強した茶抽出物が得られる。このテアニン高含有茶抽出物中のテアニン量は、アミノ酸の総量に対してテアニンの割合が0.1以上、好ましくは0.15以上となるように添加するのが好ましい。または、テアニン高含有茶抽出物中の茶葉由来固形分に対し、テアニンの割合が0.3重量%以上、好ましくは0.6重量%以上、より好ましくは0.8重量%以上、さらにより好ましくは1.0重量%以上、特に好ましくは1.5重量%以上となるように、テアニンを添加するのが好ましい。テアニンは、茶葉から分離精製された精製品や濃縮品等、市販されている粉末状、液体状もの等いずれのものを用いてもよいが、第1工程で記載したとおり、茶葉の低温抽出液にはテアニンが高濃度で含まれているので、この茶葉の低温抽出液をテアニンとして添加することもできる。この茶葉の低温抽出液を用いると、ヘキサナール等の香気成分も混合されるので、よりフレッシュな旨味と厚みのあるコク味とを付与することができる。以下に、茶葉の低温抽出液について、より詳細に説明する。
(Third step: a step of obtaining a tea extract with a high content of theanine)
The present invention provides a tea extract that enhances fresh umami in addition to rich and thick umami by mixing theanine into the tea extract (enzyme extract) obtained by the above enzyme extraction. can get. The theanine content in this tea extract with a high content of theanine is preferably added so that the theanine content is 0.1 or more , preferably 0.15 or more , based on the total amount of amino acids. Or, the proportion of theanine is 0.3% by weight or more, preferably 0.6% by weight or more, more preferably 0.8% by weight or more, and still more preferably, based on the tea leaf-derived solid content in the tea extract with a high content of theanine Is preferably 1.0% by weight or more, particularly preferably 1.5% by weight or more. As theanine, any commercially available powdered or liquid product such as a purified product or concentrated product separated and purified from tea leaves may be used, but as described in the first step, a low-temperature extract of tea leaves is used. Since theanine is contained in a high concentration, the tea leaf low-temperature extract can be added as theanine. When this low-temperature extract of tea leaves is used, aromatic components such as hexanal are also mixed, so that a fresher umami taste and a thick body can be imparted. Below, the low temperature extract of tea leaves is demonstrated in detail.

茶葉の低温抽出液の原料となる茶葉としては、煎茶、番茶、ほうじ茶、玉露、かぶせ茶、甜茶等の蒸し製の不発酵茶(緑茶);嬉野茶、青柳茶、各種中国茶等の釜炒茶等の不発酵茶;包種茶、鉄観音茶、ウーロン茶等の半発酵茶;紅茶、阿波番茶、プアール茶などの発酵茶等、いずれのものも用いることができる。なかでも、特に旨味やコク味が重要視される不発酵茶および半発酵茶が好適に用いられる。また、嗜好性にもよるが、上述の酵素抽出液と同じ種類の原料茶葉を用いることが、風味の観点から好ましい。   The tea leaves that are used as the raw material for the low temperature extract of tea leaves include steamed non-fermented tea (green tea) such as Sencha, Bancha, Hojicha, Gyokuro, Kabusecha, and Kochacha; Non-fermented teas such as tea; semi-fermented teas such as baling tea, iron kannon tea, oolong tea; fermented teas such as black tea, Awaban tea, and puar tea can be used. Among these, non-fermented tea and semi-fermented tea, in which umami and rich taste are particularly important, are preferably used. Moreover, although it depends on palatability, it is preferable from a viewpoint of flavor to use the same kind of raw material tea leaves as the above-mentioned enzyme extract.

低温抽出液は、上記茶葉を低温の溶媒にて抽出することにより得られる。ここで、低温とは、0〜40℃、好ましくは10〜30℃程度をいう。低温での抽出は、原料茶葉のフレッシュな旨味成分(ヘキサナール等の香気成分を含む)を選択的かつ効率よく取り出すことができる。上述のとおり、このフレッシュな旨味成分にはテアニンが該当し、このテアニンは、低温で抽出される成分である。
抽出溶媒は、食品として利用可能なものであれば特に限定されず、蒸留水、脱塩水、水道水、アルカリイオン水、海洋深層水、イオン交換水、脱酸素水や、含水アルコール(10〜90v/v%アルコール)、無機塩類を含有する水などを用いることができるが、特に純水やイオン交換水を用いることが好ましい。これは、水中にカルシウムイオンや鉄イオン等が溶解している場合、茶葉抽出液中のタンニンと結合を生じ、不溶解物を生じたり、色の変化が生じたりすることがあるからである。
The low temperature extract is obtained by extracting the tea leaves with a low temperature solvent. Here, low temperature means 0-40 degreeC, Preferably it is about 10-30 degreeC. Extraction at a low temperature can selectively and efficiently take out fresh umami components (including aroma components such as hexanal) of the raw tea leaves. As described above, theanine corresponds to this fresh umami component, and this theanine is a component extracted at a low temperature.
The extraction solvent is not particularly limited as long as it can be used as a food. Distilled water, demineralized water, tap water, alkaline ionized water, deep sea water, ion exchanged water, deoxygenated water, hydrous alcohol (10 to 90 v) / V% alcohol), water containing inorganic salts, and the like can be used, but it is particularly preferable to use pure water or ion-exchanged water. This is because when calcium ions, iron ions, or the like are dissolved in water, they may bind to tannins in the tea leaf extract, resulting in insoluble matters or color changes.

抽出溶媒の使用量は、用いる茶葉の種類や抽出溶媒の種類、抽出温度、所望される嗜好性等により異なるが、通常、茶葉の重量を基準として、5〜50重量部程度である。
また、抽出時間も適宜設定すればよく、通常、5〜30分程度、より好ましくは10〜20分程度である。本発明者らの検討によると、低温抽出を行った場合、カテキン類よりもアミノ酸が早く浸出し、茶葉の10倍量のイオン交換水(25℃)で抽出した際には、約10分程度でアミノ酸の全量を抽出できること、アミノ酸が全量抽出された後は、カテキン類の浸出する割合が高くなることを確認している。したがって、アミノ酸の全量が抽出された時点で抽出を終了するのが、最も好ましい。アミノ酸の全量が抽出されたかどうかは、HPLC等を用いて抽出液のアミノ酸含量を経時的に測定し、アミノ酸の溶出がみられなくなった時点により判断できる(参考例1参照)。
本発明の低温抽出における抽出方法も何ら限定されるものではなく、公知の方法を用いることができる。例えば、茶葉と溶媒とをタンクに入れて抽出し、次いで篩により茶葉から抽出液を液切りし、必要に応じて遠心分離、濾過等を行い抽出液を得る方法(ニーダー抽出とも呼ばれる)や、茶葉に溶媒を通液して原料中を通過させて抽出する通液式抽出が挙げられる。抽出効率の観点から、上記の通液式抽出が好適に用いられる。この通液式抽出における抽出方法は特に限定されず、シャワー流下するいわゆるドリップ式抽出や、カラム抽出等いずれの方式もとることが可能であるが、カラム抽出の場合は、例えば下から上へ通液するアップフロー方式が、抽出効率や抽出時のメッシュ詰まりが生じ難いという観点から好ましい。なお、この際、茶葉は、通常、金属製のメッシュの上に置かれるが、金属製メッシュでなく、布やペーパーなど、茶葉層を支え、茶葉から抽出液が分離できるものであればよい。なお、抽出の際は、抽出機内を密閉にして圧力をかける抽出を行ってもよく、また、酸化防止剤等の添加剤を混合してもよい。
The amount of extraction solvent used varies depending on the type of tea leaf used, the type of extraction solvent, the extraction temperature, the desired palatability, etc., but is usually about 5 to 50 parts by weight based on the weight of the tea leaf.
Moreover, what is necessary is just to set extraction time suitably, Usually, about 5 to 30 minutes, More preferably, it is about 10 to 20 minutes. According to the study by the present inventors, when low-temperature extraction is performed, amino acids are leached faster than catechins, and when extracted with 10 times the amount of ion-exchanged water (25 ° C.) of tea leaves, about 10 minutes. It has been confirmed that the total amount of amino acids can be extracted with, and that the leaching rate of catechins increases after the total amount of amino acids has been extracted. Therefore, it is most preferable to end the extraction when the total amount of amino acids is extracted. Whether or not the total amount of amino acids has been extracted can be determined by measuring the amino acid content of the extract over time using HPLC or the like, and when elution of amino acids is no longer observed (see Reference Example 1).
The extraction method in the low temperature extraction of the present invention is not limited at all, and a known method can be used. For example, the tea leaves and the solvent are extracted by putting them in a tank, and then the extract is drained from the tea leaves with a sieve, and if necessary, the extract is obtained by centrifugation, filtration, etc. (also called kneader extraction), There is a liquid extraction method in which a solvent is passed through tea leaves and extracted through the raw material. From the viewpoint of extraction efficiency, the above-described liquid extraction is preferably used. The extraction method in this liquid extraction is not particularly limited, and any method such as a so-called drip extraction in which a shower flows down or a column extraction can be used. In the case of column extraction, for example, the extraction is performed from bottom to top. The liquid upflow method is preferable from the viewpoint of extraction efficiency and the difficulty of mesh clogging during extraction. In this case, the tea leaves are usually placed on a metal mesh, but may be any material that supports the tea leaf layer and can separate the extract from the tea leaves, such as cloth or paper, instead of the metal mesh. In addition, at the time of extraction, the inside of an extractor may be sealed and the extraction which applies a pressure may be performed, and additives, such as antioxidant, may be mixed.

得られた低温抽出液は、必要に応じて、遠心分離、濾過等の分離操作を行って、清澄度を高めることもできる。また、濃縮操作を行って濃縮液の形態とすることもできる。
このようにして得られる低温抽出液には、アミノ酸のなかでもフレッシュな旨味成分であるテアニンを豊富に含有する。テアニンの含量は多いほど好ましいが、一般に、茶葉10gあたり10mg以上、好ましくは15mg以上、より好ましくは20mg以上となるように抽出するとよく、茶葉由来の可溶性固形分( [g]=抽出液総量[g]×Brix[%]/100)全体に対する割合として、0.8重量%以上、好ましくは1.0重量%以上、より好ましくは1.5重量%以上、さらに好ましくは2.0重量%以上、特に好ましくは2.5重量%以上となるように抽出する。
本発明では、上述のとおり、酵素抽出液に低温抽出液を混合することで、より香味に優れた茶抽出物とすることができる。具体的には、アミノ酸を高濃度で含有しコク及び厚みのある旨味の酵素抽出液と、フレッシュな旨味成分であるテアニンを豊富に含有する低温抽出液とを混合することで、フレッシュかつコク・厚みを有する豊かな旨味の茶抽出物が得られる。
The obtained low-temperature extract may be subjected to a separation operation such as centrifugation or filtration, if necessary, to increase the clarity. Moreover, it can also be made into the form of a concentrate by performing concentration operation.
The low-temperature extract thus obtained contains abundantly theanine which is a fresh umami component among amino acids. The theanine content is preferably as high as possible, but in general, extraction should be performed so that the amount is 10 mg or more, preferably 15 mg or more, more preferably 20 mg or more per 10 g of tea leaves, and soluble solid content derived from tea leaves ([g] = total amount of extract [ g] × Brix [%] / 100) as a proportion of the whole, 0.8% by weight or more, preferably 1.0% by weight or more, more preferably 1.5% by weight or more, and further preferably 2.0% by weight or more. Particularly preferably, the extraction is performed so as to be 2.5% by weight or more.
In this invention, it can be set as the tea extract which was more excellent in flavor by mixing a low temperature extract with an enzyme extract as above-mentioned. Specifically, by mixing a rich and thick umami enzyme extract containing a high concentration of amino acids with a low-temperature extract rich in theanine, a fresh umami ingredient, fresh and rich A rich umami tea extract having a thickness is obtained.

この配合割合は、得られるテアニン高含有茶抽出物中のテアニン含量が、アミノ酸の総量に対して0.1以上、好ましくは0.15以上となるようになるのであれば、またはテアニン高含有茶抽出物中の茶葉由来固形分に対し、テアニンの割合が0.3重量%以上、好ましくは0.6重量%以上、より好ましくは0.8重量%以上、さらにより好ましくは1.0重量%以上、特に好ましくは1.5重量%以上となるようになるのであれば、特に制限されず、所望する嗜好に応じて適宜選択すればよいが、茶葉の有効な成分を確保するために、酵素抽出液および低温抽出液の全量を用いるのが好ましい。この際、酵素抽出液と低温抽出液の容量割合は、通常、1:0.1〜15、好ましくは1:2〜10程度である。
混合された茶抽出物におけるアミノ酸含量は、茶葉10gあたり160mg以上、好ましくは180mg以上、より好ましくは200mg以上であり、茶葉由来の可溶性固形分( [g]=抽出液総量[g]×Brix[%]/100)全体に対する割合として、2.5重量%以上、好ましくは5.0重量%以上、より好ましくは7.0重量%である。また、テアニンの含量は、茶葉10gあたり10mg以上、好ましくは15mg以上、より好ましくは20mg以上であり、茶葉由来の可溶性固形分( [g]=抽出液総量[g]×Brix[%]/100)全体に対する割合として、0.3重量%以上、好ましくは0.6重量%以上、より好ましくは0.8重量%以上、さらに好ましくは1.0重量%以上、特に好ましくは1.5重量%以上である。
This blending ratio is such that the theanine content in the obtained tea extract with a high content of theanine is 0.1 or more , preferably 0.15 or more with respect to the total amount of amino acids, or the tea with a high content of theanine. The theanine content of the tea leaf-derived solid content in the extract is 0.3% by weight or more, preferably 0.6% by weight or more, more preferably 0.8% by weight or more, and even more preferably 1.0% by weight. As described above, it is not particularly limited as long as it is preferably 1.5% by weight or more, and may be appropriately selected according to the desired taste. In order to ensure an effective component of tea leaves, It is preferable to use the entire amount of the extract and the low temperature extract. Under the present circumstances, the volume ratio of an enzyme extract and a low temperature extract is about 1: 0.1-15 normally, Preferably it is about 1: 2-10.
The amino acid content in the mixed tea extract is 160 mg or more per 10 g of tea leaves, preferably 180 mg or more, more preferably 200 mg or more, and soluble solid content derived from tea leaves ([g] = total amount of extract [g] × Brix [ %] / 100) as a proportion of the whole, is 2.5% by weight or more, preferably 5.0% by weight or more, more preferably 7.0% by weight. The theanine content is 10 mg or more per 10 g of tea leaves, preferably 15 mg or more, more preferably 20 mg or more, and soluble solid content derived from tea leaves ([g] = total amount of extract [g] × Brix [%] / 100 ) 0.3% by weight or more, preferably 0.6% by weight or more, more preferably 0.8% by weight or more, still more preferably 1.0% by weight or more, and particularly preferably 1.5% by weight as a percentage of the whole. That's it.

一方、カテキン類の含量は、茶葉10gあたり800mg以下、好ましくは700mg以下であり、茶葉由来の可溶性固形分( [g]=抽出液総量[g]×Brix[%]/100)全体に対する割合として、15.0重量%以下、好ましくは13.5重量%以下、より好ましくは10.0重量%以下、特に好ましくは8.0重量%以下である。 後述するが、本発明者らの検討によると、酵素抽出液に茶葉の低温抽出液を混合して調製した茶抽出物について、茶葉由来の固形分あたりのアミノ酸の総量が2.5重量%以上の茶抽出物に、コク・厚みのある旨みがあることを確認している。そして、このアミノ酸を高濃度で含有する茶抽出物のうち、カテキン含量(カテキンの総量)が15.0を超えるものにはやや苦渋味が感じられた(比較例A1参照)が、15.0以下のものでアミノ酸含量(アミノ酸の総量)が5.0重量%を超えるものには苦渋味がなく(比較例A1’、実施例C3参照)、特にアミノ酸含量が7.0重量%以上のものには豊かな旨みがあること(実施例D4’、E4参照)、カテキン含量が15.0以下であってもアミノ酸含量が5.0以下のものはやや苦渋みが感じられること(実施例B3、D4参照)を確認している。   On the other hand, the content of catechins is 800 mg or less per 10 g of tea leaves, preferably 700 mg or less, as a ratio to the soluble solid content derived from tea leaves ([g] = total amount of extract [g] × Brix [%] / 100). It is 15.0% by weight or less, preferably 13.5% by weight or less, more preferably 10.0% by weight or less, and particularly preferably 8.0% by weight or less. As will be described later, according to the study by the present inventors, the total amount of amino acids per solid content derived from tea leaves is 2.5% by weight or more for the tea extract prepared by mixing the tea extract with the low temperature extract of tea leaves. It has been confirmed that the tea extract has a rich and thick flavor. Of the tea extracts containing this amino acid at a high concentration, those having a catechin content (total amount of catechin) exceeding 15.0 felt a bitter bitter taste (see Comparative Example A1). Those having the amino acid content (total amount of amino acids) exceeding 5.0% by weight have no bitter taste (see Comparative Example A1 ′ and Example C3), and particularly those having an amino acid content of 7.0% by weight or more Has a rich umami (see Examples D4 ′ and E4), and even if the catechin content is 15.0 or less, those having an amino acid content of 5.0 or less have a slight bitterness (Example B3). , See D4).

得られた茶抽出物は、必要に応じて、添加物を添加してもよい。添加物としては、アスコルビン酸またはその塩、pH調整剤、香料、および着色料等を挙げることができる。
また、上記茶抽出物は、遠心分離、濾過等の分離操作を行って、清澄度を高めることもできる。また、濃縮操作や乾燥操作を行って濃縮液の形態や乾燥物の形態(粉末)とすることもできる。本発明者らは、酵素抽出液に茶葉の低温抽出液を混合して調製したテアニン高含有茶抽出物を濃縮して調製した濃縮液、及びこの濃縮液を凍結乾燥してパウダー状にした後、再度水に溶解して調製した茶抽出液(還元)について、風味が良好であることを確認している。
An additive may be added to the obtained tea extract as necessary. Examples of the additive include ascorbic acid or a salt thereof, a pH adjuster, a fragrance, and a coloring agent.
In addition, the tea extract can be subjected to a separation operation such as centrifugation or filtration to increase the clarification degree. Moreover, it can also be made into the form of a concentrate and the form (powder) of a dried material by performing concentration operation and drying operation. The inventors of the present invention have prepared a concentrated solution prepared by concentrating a tea extract containing a high amount of theanine prepared by mixing a low temperature extract of tea leaves with an enzyme extract, and after lyophilizing the concentrated solution into a powder form. The tea extract (reduced) prepared by dissolving again in water has been confirmed to have good flavor.

以下実施例により、本発明をより具体的に説明するが、本発明はこれらに限定されるものではない。以下の実施例(参考例、比較例も含む)では、火入れ度の違う2種類の茶葉(火入れ度「中」又は「弱」と表記する。)を使用した。
参考例 1
カラム型抽出機に10gの緑茶葉(火入れ度:中)を封入し、抽出機上部から25℃のイオン交換水を100mL加え、緑茶葉を浸漬させた。そこに25℃のイオン交換水を50mL/minの流量にて連続的に20分通液し、その間、下部より連続的に排出される液を2分毎にサンプリングした。その後、サンプリング液のカテキン、アミノ酸を測定した。
カテキンの測定方法にはHPLCを用いた。具体的測定方法は、以下のとおり。
(HPLC条件)
HPLC装置:TOSOH HPLCシステム LC8020 model II
カラム:TSKgel ODS80T sQA(4.6mm×150mm)
カラム温度:40℃
移動相A:水-アセトニトリル-トリフルオロ酢酸(90:10:0.05)
移動相B:水-アセトニトリル-トリフルオロ酢酸(20:80:0.05)
検出:UV275nm
注入量:20μL
流速:1mL/min.
グラジエントプログラム:
時間(分) %A %B
0 100 0
5 92 8
11 90 10
21 90 10
22 0 100
29 0 100
30 100 0
標準物質:カテキン、エピカテキン、ガロカテキン、エピガロカテキン、カテキンガレート、エピカテキンガレート、ガロカテキンガレートおよびエピガロカテキンガレート(クリタ高純度試薬)
アミノ酸の測定方法にもHPLCを用いた。具体的測定方法は、以下のとおり。
(HPLC条件)
HPLC装置:Waters アミノ酸分析装置2695
カラム:AccQ-Tagカラム(3.9mm×150mm)
カラム温度:40℃
移動相A:AccQ-TagA(pH5.8)
移動相B:アセトニトリル
移動層C:水/メタノール=9/1
検出:EX250nm EM395nm Gain100
注入量:5μL
グラジエントプログラム:
時間(分) 流速(ml/min) %A %B %C
0 1 100 0 0
1 1 99 1 0
16 1 97 3 0
25 1 94 6 0
35 1 86 14 0
40 1 86 14 0
50 1 82 18 0
51 1 0 60 40
54 1 100 0 0
75 1 0 60 40
110 0 0 60 40
標準物質:アミノ酸18種(アルギニン、リジン、ヒスチジン、フェニルアラニン、チロシン、ロイシン、イソロイシン、メチオニン、バリン、アラニン、グリシン、プロリン、グルタミン酸、セリン、スレオニン、アルパラギン酸、トリプトファン、シスチン)およびテアニン
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples. In the following examples (including reference examples and comparative examples), two types of tea leaves (indicated as “medium” or “weak”) were used.
Reference example 1
A column-type extractor was filled with 10 g of green tea leaves (degree of fire: medium), 100 mL of 25 ° C. ion exchange water was added from the top of the extractor, and the green tea leaves were immersed. 25 ° C. ion exchange water was continuously passed at a flow rate of 50 mL / min for 20 minutes, and during that time, the liquid continuously discharged from the lower part was sampled every 2 minutes. Thereafter, catechin and amino acid in the sampling solution were measured.
HPLC was used for the measurement method of catechin. The specific measurement method is as follows.
(HPLC conditions)
HPLC apparatus: TOSOH HPLC system LC8020 model II
Column: TSKgel ODS80T sQA (4.6 mm x 150 mm)
Column temperature: 40 ° C
Mobile phase A: water-acetonitrile-trifluoroacetic acid (90: 10: 0.05)
Mobile phase B: water-acetonitrile-trifluoroacetic acid (20: 80: 0.05)
Detection: UV275nm
Injection volume: 20 μL
Flow rate: 1 mL / min.
Gradient program:
Time (min)% A% B
0 100 0
5 92 8
11 90 10
21 90 10
22 0 100
29 0 100
30 100 0
Standard substances: catechin, epicatechin, gallocatechin, epigallocatechin, catechin gallate, epicatechin gallate, gallocatechin gallate and epigallocatechin gallate (Kurita high purity reagent)
HPLC was also used as a method for measuring amino acids. The specific measurement method is as follows.
(HPLC conditions)
HPLC device: Waters amino acid analyzer 2695
Column: AccQ-Tag column (3.9 mm x 150 mm)
Column temperature: 40 ° C
Mobile phase A: AccQ-TagA (pH 5.8)
Mobile phase B: acetonitrile Mobile bed C: water / methanol = 9/1
Detection: EX250nm EM395nm Gain100
Injection volume: 5 μL
Gradient program:
Time (min) Flow rate (ml / min)% A% B% C
0 1 100 0 0
1 1 99 1 0
16 1 97 3 0
25 1 94 6 0
35 1 86 14 0
40 1 86 14 0
50 1 82 18 0
51 1 0 60 40
54 1 100 0 0
75 1 0 60 40
110 0 0 60 40
Standard substances: 18 amino acids (arginine, lysine, histidine, phenylalanine, tyrosine, leucine, isoleucine, methionine, valine, alanine, glycine, proline, glutamic acid, serine, threonine, aspartic acid, tryptophan, cystine) and theanine

結果を図1に示す。図1より、アミノ酸はカテキン類(図中、カテキンと表記)よりも早いタイミングで緑茶葉より抽出され、10分頃にはほぼ全量が抽出されることがわかった。一方、カテキン類は20分経過しても一部残存することがわかった。低温抽出で抽出時間を選択することにより、カテキン類(渋み成分)の抽出を抑制し、アミノ酸(旨味成分)を選択的に抽出できることが確認された。   The results are shown in FIG. From FIG. 1, it was found that amino acids were extracted from green tea leaves at an earlier timing than catechins (denoted as catechin in the figure), and almost all of them were extracted around 10 minutes. On the other hand, it was found that some catechins remained even after 20 minutes. By selecting the extraction time by low temperature extraction, it was confirmed that extraction of catechins (astringency components) can be suppressed and amino acids (umami components) can be selectively extracted.

参考例 2
茶葉を緑茶葉(火入れ度:弱)にする以外は、参考例1と同様にして低温抽出液を得、アミノ酸及びカテキンの分析を行った。緑茶葉を変更しても、アミノ酸がカテキン類よりも早く抽出されることが確認され、参考例1と同様に、10分頃にはアミノ酸のほぼ全量が抽出された。このときの抽出液中のアミノ酸量は、167mgであった。
比較例1
まず、第一工程としてカラム型抽出機に10gの緑茶葉(火入れ度:中)を封入し、抽出機上部から25℃のイオン交換水を100mL加え、緑茶葉を浸漬させた。そこに25℃のイオン交換水を50mL/minの流量にて連続的に20分通液し、低温抽出液を得た(試料A1)。次に試料A1を抽出した後の抽出残渣に、プロテアーゼ及びペクチナーゼを各0.2gずつ添加し、40℃のイオン交換水を加え総重量160gに調整し、40℃に保持したまま50mL/minにて16時間循環通液を行い、酵素反応を行った。得られた酵素処理液を90℃10分加熱し酵素を失活させ、酵素反応液を得た(試料A2)。さらに、上記試料A1全量及びA2全量を混合し、茶抽出物を得た(試料A3)。
試料A1〜試料A3におけるアミノ酸及びカテキン類の含量を参考例1と同様に分析した。また、各試料の香味について、専門パネラー3名で評価した。
Reference example 2
A low temperature extract was obtained and analyzed for amino acids and catechins in the same manner as in Reference Example 1 except that the tea leaves were changed to green tea leaves (degree of fire: weak). Even when the green tea leaves were changed, it was confirmed that amino acids were extracted earlier than catechins. As in Reference Example 1, almost all amino acids were extracted around 10 minutes. The amount of amino acid in the extract at this time was 167 mg.
Comparative Example 1
First, as a first step, 10 g of green tea leaves (degree of fire: medium) were sealed in a column type extractor, and 100 mL of 25 ° C. ion exchange water was added from the top of the extractor to immerse the green tea leaves. Thereto, 25 ° C. ion-exchanged water was continuously passed at a flow rate of 50 mL / min for 20 minutes to obtain a low-temperature extract (sample A1). Next, 0.2 g each of protease and pectinase is added to the extraction residue after extracting the sample A1, and the total weight is adjusted to 160 g by adding ion exchange water at 40 ° C., and is kept at 40 ° C. to 50 mL / min. Then, circulation was conducted for 16 hours to carry out enzyme reaction. The obtained enzyme treatment liquid was heated at 90 ° C. for 10 minutes to deactivate the enzyme, thereby obtaining an enzyme reaction liquid (sample A2). Further, the total amount of Sample A1 and the total amount of A2 were mixed to obtain a tea extract (Sample A3).
The contents of amino acids and catechins in Sample A1 to Sample A3 were analyzed in the same manner as in Reference Example 1. In addition, the flavor of each sample was evaluated by three specialized panelists.

結果を表1に示す。回収液量(収量)は、試料A1が972g、試料A2が130gであった。また、アミノ酸の含量は、試料A1が57mg、試料A2が103mgであった。この結果と参考例とを合わせて考察すると、第一工程でアミノ酸がほぼ全量抽出されていたが、第二工程の酵素処理におけるタンパクの分解によってさらにアミノ酸の生成量が増加したと考えられる。
一方、カテキン類の含量は、試料A1が671mg、試料A2が171mgであった。参考例と合わせて考察すると、第一工程で抽出されなかったカテキン類が第二工程によって更に抽出されたと考えられる。また、試料A2のアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、0.60であった。
また、香味評価の結果、試料A1と試料A2では旨みの特徴が異なり、試料A1はフレッシュ感のある旨みであるのに対し、試料A2はコク・厚みのある旨みであった。また、試料A2ではカテキン類由来と思われる苦渋味がやや感じられた。さらに、試料A1と試料A2を混合した液(試料A3)は、二つの液の香味の特徴を有する、すなわちフレッシュかつコク・厚みのある旨みを有するものであることがわかった。しかし、やや苦渋味が感じられた。
The results are shown in Table 1. The amount of recovered liquid (yield) was 972 g for sample A1 and 130 g for sample A2. The amino acid content was 57 mg for sample A1 and 103 mg for sample A2. Considering this result together with the reference example, almost all amino acids were extracted in the first step, but it is considered that the amount of amino acids produced was further increased by the degradation of the protein in the enzyme treatment in the second step.
On the other hand, the content of catechins was 671 mg for sample A1 and 171 mg for sample A2. Considering together with the reference example, it is considered that catechins that were not extracted in the first step were further extracted in the second step. Moreover, it was 0.60 when the ratio (a / b) of the amino acid (a) and catechin (b) of sample A2 was calculated.
Further, as a result of the flavor evaluation, sample A1 and sample A2 had different umami characteristics. Sample A1 had a fresh umami, while sample A2 had a rich and thick umami. In Sample A2, a bitter and astringent taste that seems to be derived from catechins was slightly felt. Further, it was found that the liquid (sample A3) obtained by mixing the sample A1 and the sample A2 has the flavor characteristics of the two liquids, that is, has a fresh, rich and thick taste. However, a slightly bitter taste was felt.

Figure 0005238993
比較例2
茶葉を緑茶葉(火入れ度:弱)にする以外は、比較例1と同様にして低温抽出液(試料A1’)を得、次にこの抽出残渣から酵素反応液を得(試料A2’)、試料A1’と試料A2’の全量を混合して茶抽出物(試料A3’)を得た。比較例1と同様に各試料におけるアミノ酸及びカテキン量を分析し、官能評価を行った。
結果を表2に示す。回収液量(収量)は、試料A1’が462g、試料A2’が129gであった。また、アミノ酸の含量は、試料A1’が120mg、試料A2’が187mgであった。この結果と参考例とを合わせて考察すると、比較例1と同様に、第一工程でアミノ酸がほぼ全量抽出されていたが、第二工程の酵素処理におけるタンパクの分解によってさらにアミノ酸の生成量が増加したと考えられる。
Figure 0005238993
Comparative Example 2
A low temperature extract (sample A1 ′) was obtained in the same manner as in Comparative Example 1 except that the tea leaves were changed to green tea leaves (degree of fire: weak), and then an enzyme reaction solution was obtained from this extraction residue (sample A2 ′). The whole amount of sample A1 ′ and sample A2 ′ was mixed to obtain a tea extract (sample A3 ′). In the same manner as in Comparative Example 1, the amount of amino acid and catechin in each sample was analyzed, and sensory evaluation was performed.
The results are shown in Table 2. The amount of recovered liquid (yield) was 462 g for sample A1 ′ and 129 g for sample A2 ′. The amino acid content was 120 mg for sample A1 ′ and 187 mg for sample A2 ′. Considering this result together with the reference example, almost the same amount of amino acids was extracted in the first step as in Comparative Example 1, but the amount of amino acids produced was further increased by the degradation of the protein in the enzyme treatment in the second step. It is thought that it increased.

一方、カテキン類の含量は、試料A1’が337mg、試料A2’が282mgであった。参考例と合わせて考察すると、比較例1と同様に、第一工程で抽出されなかったカテキン類が第二工程によって更に抽出されたと考えられる。また、試料A2’のアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、0.66であった。
また、香味評価の結果、第二工程で得られた酵素抽出液(試料A2’)は、カテキン類の含有量が少なく、アミノ酸を高濃度で含有するものであり、香味的にもコクと厚みのある豊かな旨味を有し、苦味・渋味の比較的少ない嗜好性の優れたものであった。さらに、試料A1’と試料A2’を混合した試料A3’は、フレッシュかつコク・厚みのある旨みを有し、かつ渋味が抑制された、従来のものとは全く違った香味を有する緑茶抽出物であった。

Figure 0005238993
実施例1.茶抽出物の製造(1)
まず、第一工程としてカラム型抽出機に10gの緑茶葉(火入れ度:弱)を封入し、抽出機上部から75℃のイオン交換水を100mL加え、緑茶葉を浸漬させた。そこに75℃のイオン交換水を50mL/minの流量にて連続的に70分通液し、高温抽出液を得た(試料B1)。次に試料B1を抽出した後の抽出残渣に、プロテアーゼ及びペクチナーゼを各0.2gずつ添加し、40℃のイオン交換水を加え総重量160gに調整し、40℃に保持したまま50mL/minにて16時間循環通液を行い、酵素反応を行った。得られた酵素処理液を90℃10分加熱し酵素を失活させ、酵素反応液を得た(試料B2)。さらに、上記試料B1全量及びB2全量を混合し、茶抽出物を得た(試料B3)。
試料B1〜試料B3におけるアミノ酸及びカテキン類の含量を参考例1と同様に分析した。また、各試料の香味について、専門パネラー3名で評価した。 On the other hand, the content of catechins was 337 mg for sample A1 ′ and 282 mg for sample A2 ′. When considered together with the reference example, it is considered that catechins that were not extracted in the first step were further extracted in the second step, as in Comparative Example 1. Moreover, it was 0.66 when the ratio (a / b) of the amino acid (a) and catechin (b) of sample A2 'was calculated.
Moreover, as a result of the flavor evaluation, the enzyme extract (sample A2 ′) obtained in the second step has a low content of catechins and a high concentration of amino acids. It had a rich umami taste and an excellent taste with relatively little bitterness and astringency. Furthermore, sample A3 ′, which is a mixture of sample A1 ′ and sample A2 ′, has a fresh, rich and thick umami taste, and has a flavor that is completely different from the conventional one, with astringency suppressed. It was a thing.
Figure 0005238993
Example 1. Production of tea extract (1)
First, as a first step, 10 g of green tea leaves (heating degree: weak) were sealed in a column type extractor, and 100 mL of 75 ° C. ion exchange water was added from the top of the extractor to immerse the green tea leaves. Thereto, 75 ° C. ion exchange water was continuously passed at a flow rate of 50 mL / min for 70 minutes to obtain a high-temperature extract (sample B1). Next, 0.2 g each of protease and pectinase is added to the extraction residue after extracting sample B1, and the total weight is adjusted to 160 g by adding ion-exchanged water at 40 ° C., and kept at 40 ° C. to 50 mL / min. Then, circulation was conducted for 16 hours to carry out enzyme reaction. The obtained enzyme treatment liquid was heated at 90 ° C. for 10 minutes to inactivate the enzyme to obtain an enzyme reaction liquid (sample B2). Furthermore, the sample B1 whole quantity and B2 whole quantity were mixed, and the tea extract was obtained (sample B3).
The contents of amino acids and catechins in Sample B1 to Sample B3 were analyzed in the same manner as in Reference Example 1. In addition, the flavor of each sample was evaluated by three specialized panelists.

結果を表3に示す。回収液量(収量)は、試料B1が3406g、試料B2が139gであった。また、アミノ酸の含量は、試料B1が175mg、試料B2が256mgであり、カテキン類の含量は、試料B1が1083mg、試料B2が16mgであった。この結果から、第一工程(高温抽出)により、カテキン類がほぼ全量抽出されたこと、第一工程(高温抽出)で遊離のアミノ酸が抽出されるが第二工程の酵素処理におけるタンパクの分解によってさらにアミノ酸の生成量が増加したことが考察される。
比較例2における試料A2’と実施例1における試料B2では、低温抽出後の抽出残渣から酵素反応液を得たか、高温抽出後の抽出残渣から酵素反応液を得たかの違いがある。試料A1’のカテキン抽出量と試料B1のカテキン抽出量を比較すると、試料B1のカテキン抽出量が試料A1’のカテキン抽出量の約3.2倍となっている。また、試料A2’のアミノ酸量と試料B2のアミノ酸量を比較すると、試料B2のアミノ酸量が試料A2’のアミノ酸量の約1.4倍となっている。これより、酵素抽出の前に高温抽出を行う、すなわちカテキン類を除去することで、効率的に酵素反応が行われ、アミノ酸を多量に抽出できることがわかる。これは、カテキン類を除去することによって、酵素の反応が高められ、酵素の作用が十分発揮されたと考えることができる。
The results are shown in Table 3. The amount of recovered liquid (yield) was 3406 g for sample B1 and 139 g for sample B2. The amino acid content was 175 mg for sample B1 and 256 mg for sample B2, and the content of catechins was 1083 mg for sample B1 and 16 mg for sample B2. From this result, almost all catechins were extracted by the first step (high temperature extraction), and free amino acids were extracted by the first step (high temperature extraction). Furthermore, it is considered that the amount of amino acids produced has increased.
Sample A2 ′ in Comparative Example 2 and Sample B2 in Example 1 differ in whether an enzyme reaction solution is obtained from an extraction residue after low-temperature extraction or an enzyme reaction solution is obtained from an extraction residue after high-temperature extraction. Comparing the catechin extraction amount of sample A1 ′ and the catechin extraction amount of sample B1, the catechin extraction amount of sample B1 is about 3.2 times the catechin extraction amount of sample A1 ′. Further, when the amino acid amount of sample A2 ′ and the amino acid amount of sample B2 are compared, the amino acid amount of sample B2 is about 1.4 times the amino acid amount of sample A2 ′. From this, it can be seen that by performing high-temperature extraction before enzyme extraction, that is, by removing catechins, an enzyme reaction is efficiently performed and a large amount of amino acids can be extracted. It can be considered that by removing catechins, the reaction of the enzyme was enhanced and the action of the enzyme was sufficiently exerted.

なお、試料B2におけるアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、15.79であった。

Figure 0005238993
実施例2.茶抽出物の製造(2)
まず、第一工程としてビーカーに10gの緑茶葉(火入れ度:弱)を封入し、80℃の0.2%塩酸を150mL加え(pH2.0)、80℃を保った状態で5時間浸漬した後、顆粒状の水酸化ナトリウムを0.32g加え、pHを6.6に調整した(試料C1)。次に試料C1を抽出した後の抽出残渣に、プロテアーゼ及びペクチナーゼを各0.2gずつ添加し、40℃のイオン交換水を加え総重量160gに調整し、40℃に保持したまま50mL/minにて16時間循環通液を行い、酵素反応を行った。得られた酵素処理液を90℃10分加熱し酵素を失活させ、酵素反応液を得た(試料C2)。さらに、上記試料C1全量及びC2全量を混合し、茶抽出物を得た(試料C3)。
試料C1〜試料C3におけるアミノ酸及びカテキン類の含量を参考例1と同様に分析した。また、各試料の香味について、専門パネラー3名で評価した。
結果を表4に示す。回収液量(収量)は、試料C1が252g、試料C2が129gであった。また、アミノ酸の含量は、試料C1が172mg、試料C2が325mgであり、カテキン類の含量は、試料C1が442mg、試料C2が203mgであった。この結果から、第一工程(酸液処理)によりカテキン類が多量に抽出されたこと、第一工程(酸処理)で遊離のアミノ酸が抽出されるが第二工程の酵素処理におけるタンパクの分解によってさらにアミノ酸の生成量が増加したことが考察される。
比較例2における試料A1’と実施例2における試料C1のカテキン類の抽出量を比較すると、試料C1のカテキン抽出量が試料A1’のカテキン抽出量の約1.3倍となっている。また、比較例2における試料A2’のアミノ酸量を比較すると、試料C2のアミノ酸量が試料A2’のアミノ酸量の約1.7倍となっている。比較例2における試料A2’と実施例2における試料C2とでは、酵素抽出の前にカテキン類を除去する工程(弱酸液処理)があるかないかの違いがある。実施例2からも、酵素抽出の前にカテキン類を除去することで、効率的に酵素反応が行われ、アミノ酸を多量に抽出できることがわかる。
なお、試料C2のアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、1.60であった。 In addition, it was 15.79 when the ratio (a / b) of the amino acid (a) and catechin (b) in sample B2 was calculated.
Figure 0005238993
Example 2 Production of tea extract (2)
First, as a first step, 10 g of green tea leaves (heating degree: weak) were sealed in a beaker, 150 mL of 80% 0.2% hydrochloric acid was added (pH 2.0), and immersed for 5 hours while maintaining 80 ° C. Thereafter, 0.32 g of granular sodium hydroxide was added to adjust the pH to 6.6 (Sample C1). Next, 0.2 g each of protease and pectinase is added to the extraction residue after extracting sample C1, and ion exchange water at 40 ° C. is added to adjust the total weight to 160 g, and the mixture is kept at 40 ° C. to 50 mL / min. Then, circulation was conducted for 16 hours to carry out enzyme reaction. The obtained enzyme treatment liquid was heated at 90 ° C. for 10 minutes to deactivate the enzyme, and an enzyme reaction liquid was obtained (sample C2). Further, the sample C1 total amount and the C2 total amount were mixed to obtain a tea extract (sample C3).
The contents of amino acids and catechins in Sample C1 to Sample C3 were analyzed in the same manner as in Reference Example 1. In addition, the flavor of each sample was evaluated by three specialized panelists.
The results are shown in Table 4. The amount of recovered liquid (yield) was 252 g for sample C1 and 129 g for sample C2. The amino acid content was 172 mg for sample C1 and 325 mg for sample C2, and the content of catechins was 442 mg for sample C1 and 203 mg for sample C2. From this result, a large amount of catechins was extracted in the first step (acid solution treatment), and free amino acids were extracted in the first step (acid treatment). Furthermore, it is considered that the amount of amino acids produced has increased.
When comparing the extracted amount of catechins of sample A1 ′ in comparative example 2 and sample C1 in example 2, the extracted amount of catechin in sample C1 is about 1.3 times the extracted amount of catechin in sample A1 ′. Moreover, when the amino acid amount of sample A2 'in the comparative example 2 is compared, the amino acid amount of sample C2 is about 1.7 times the amino acid amount of sample A2'. There is a difference between Sample A2 ′ in Comparative Example 2 and Sample C2 in Example 2 whether or not there is a step (weak acid solution treatment) for removing catechins before enzyme extraction. Also from Example 2, it can be seen that by removing catechins prior to enzyme extraction, an enzyme reaction is efficiently performed and a large amount of amino acids can be extracted.
In addition, it was 1.60 when the ratio (a / b) of the amino acid (a) and catechin (b) of sample C2 was calculated.

Figure 0005238993
実施例3.茶抽出物の製造(3)
まず、第一工程としてカラム型抽出機に10gの緑茶葉(火入れ度:中)を封入し、抽出機上部から25℃のイオン交換水を100mL加え、緑茶葉を浸漬させた。そこに25℃のイオン交換水を50mL/minの流量にて連続的に20分通液し、低温抽出液を得た(試料D1)。次に第二工程として、試料D1抽出後の抽出残渣に75℃のイオン交換水を100mL加えた上で、75℃のイオン交換水を50mL/minの流量にて連続的に40分通液し、高温抽出液を得た(試料D2)。次に第三工程として、試料D2抽出後の抽出残渣に、酵素としてプロテアーゼ及びペクチナーゼを各0.2gずつ添加し、40℃のイオン交換水を加え総重量160gに調整し、40℃に保持したまま50mL/minにて16時間循環通液を行い、酵素処理(反応)を行った。その後、得られた酵素処理液を90℃で10分加熱して酵素を失活させ、酵素抽出液を得た(試料D3)。第四工程として、上記試料D1及びD3全量を混合し、茶抽出物を得た(試料D4)。
試料D1〜D4について、参考例1と同様にして、アミノ酸及びカテキン類の含量を分析した。また、専門パネラー3名により香味評価を実施した。
Figure 0005238993
Example 3 Production of tea extract (3)
First, as a first step, 10 g of green tea leaves (degree of fire: medium) were sealed in a column type extractor, and 100 mL of 25 ° C. ion exchange water was added from the top of the extractor to immerse the green tea leaves. Thereto, 25 ° C. ion exchange water was continuously passed at a flow rate of 50 mL / min for 20 minutes to obtain a low-temperature extract (sample D1). Next, as a second step, 100 mL of 75 ° C. ion exchange water is added to the extraction residue after sample D1 extraction, and then 75 ° C. ion exchange water is continuously passed at a flow rate of 50 mL / min for 40 minutes. A high temperature extract was obtained (sample D2). Next, as a third step, 0.2 g each of protease and pectinase as enzymes are added to the extraction residue after sample D2 extraction, ion-exchanged water at 40 ° C. is added to adjust the total weight to 160 g, and the temperature is maintained at 40 ° C. The solution was circulated for 16 hours at 50 mL / min and subjected to enzyme treatment (reaction). Thereafter, the obtained enzyme treatment liquid was heated at 90 ° C. for 10 minutes to deactivate the enzyme, thereby obtaining an enzyme extract (sample D3). As a 4th process, the said sample D1 and D3 whole quantity was mixed and the tea extract was obtained (sample D4).
Samples D1 to D4 were analyzed for the content of amino acids and catechins in the same manner as in Reference Example 1. In addition, flavor evaluation was carried out by three specialized panelists.

結果を表5に示す。第二工程で得られた高温抽出液(試料D2)は、本発明では廃棄する抽出液であり、アミノ酸をほとんど含有せず、カテキン類のみを含有するものであり、香味評価の結果も苦渋みを有し出涸らし様の不快臭を感じるものであった。一方、第三工程で得られた酵素抽出液(試料D3)は、カテキン類をほとんど含まず、アミノ酸を高濃度で含有するものであり、香味的にもコクと厚みのある豊かな旨味を有し、苦味・渋味のほとんどない嗜好性の優れたものであった。また、試料D3のアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、15.13であった。この結果から、第二工程でカテキン類を除去することにより、第三工程で得られる酵素抽出液(試料D3)のカテキン類の含量が抑えられたと考えられる。
さらに、試料D1と試料D3を混合した試料D4は、複雑な旨味を有し、かつ渋味が抑制された、従来のものとは全く違った香味を有する緑茶抽出物であった。

Figure 0005238993
The results are shown in Table 5. The high-temperature extract (sample D2) obtained in the second step is an extract to be discarded in the present invention, contains almost no amino acids, contains only catechins, and the results of flavor evaluation are also bitter. It had a feeling of unpleasant odor. On the other hand, the enzyme extract (sample D3) obtained in the third step contains almost no catechins, contains amino acids at a high concentration, and has a rich and rich umami flavor. However, it had excellent bitterness with little bitterness and astringency. Moreover, it was 15.13 when the ratio (a / b) of the amino acid (a) of sample D3 and catechin (b) was computed. From this result, it is considered that the content of catechins in the enzyme extract (sample D3) obtained in the third step was suppressed by removing catechins in the second step.
Furthermore, sample D4 obtained by mixing sample D1 and sample D3 was a green tea extract having a complex umami taste and astringency that was completely different from the conventional one, with astringency suppressed.
Figure 0005238993

比較例1における酵素反応液である試料A2と実施例3における酵素反応である試料D3とでは、酵素抽出の前にカテキン類を除去する工程があるかないかの違いがある。試料A2と試料D3のアミノ酸含量を比較すると、試料D3のアミノ酸含量が試料A2の約1.5倍となっていることから、酵素抽出の前にカテキン類を除去することで、効率的に酵素反応が行われ、アミノ酸を多量に抽出できることがわかる。これは、カテキン類を除去することによって、酵素の反応が高められ、酵素の作用が十分発揮されたと考えることができる。
実施例4.茶抽出物の製造(4)
茶葉を緑茶葉(火入れ度:弱)にする以外は、実施例3と同様にして低温抽出液(試料D1’)を得、次にこの抽出残渣から高温抽出液(試料D2’)を得、この抽出残渣から酵素反応液を得(試料D3’)、試料D1’及び試料D3’の全量を混合して茶抽出物(試料D4’)を得た。実施例3と同様に各試料におけるアミノ酸及びカテキン量を分析し、専門パネラー3面により官能評価を実施した。
結果を表6に示す。回収液量(収量)は、試料D1’が461g、試料D2’が2945g、試料D3’が139gであった。また、アミノ酸の含量は、試料D1’が167mg、試料D2’が8mg、試料D3’が256mgであった。この結果と参考例とを合わせて考察すると、第一工程でアミノ酸がほぼ全量抽出されていたが、第三工程の酵素処理におけるタンパクの分解によってさらにアミノ酸の生成量が増加したと考えられる。
一方、カテキン類の含量は、試料D1’が507mg、試料D2’が576mg、試料D3’が16mgであった。参考例と合わせて考察すると、第一工程で残ったカテキン類が、第二工程でほぼ全量抽出されたと考えられる。また、試料D3’のアミノ酸(a)とカテキン類(b)の比率(a/b)を算出すると、15.79であった。

Figure 0005238993
There is a difference between the sample A2 which is an enzyme reaction solution in Comparative Example 1 and the sample D3 which is an enzyme reaction in Example 3 whether or not there is a step of removing catechins before enzyme extraction. Comparing the amino acid contents of sample A2 and sample D3, the amino acid content of sample D3 is about 1.5 times that of sample A2. Therefore, by removing catechins before enzyme extraction, the enzyme can be efficiently removed. It is understood that a large amount of amino acids can be extracted by the reaction. It can be considered that by removing catechins, the reaction of the enzyme was enhanced and the action of the enzyme was sufficiently exerted.
Example 4 Production of tea extract (4)
A low temperature extract (sample D1 ′) is obtained in the same manner as in Example 3 except that the tea leaves are green tea leaves (degree of fire: weak), and then a high temperature extract (sample D2 ′) is obtained from this extraction residue, An enzyme reaction solution was obtained from this extraction residue (sample D3 ′), and the whole amount of sample D1 ′ and sample D3 ′ was mixed to obtain a tea extract (sample D4 ′). In the same manner as in Example 3, the amounts of amino acids and catechins in each sample were analyzed, and sensory evaluation was performed using three specialized panelists.
The results are shown in Table 6. The amount of recovered liquid (yield) was 461 g for sample D1 ′, 2945 g for sample D2 ′, and 139 g for sample D3 ′. The amino acid content was 167 mg for sample D1 ′, 8 mg for sample D2 ′, and 256 mg for sample D3 ′. Considering this result together with the reference example, almost all amino acids were extracted in the first step, but it is considered that the amount of amino acids produced was further increased by the degradation of the protein in the enzyme treatment in the third step.
On the other hand, the content of catechins was 507 mg for sample D1 ′, 576 mg for sample D2 ′, and 16 mg for sample D3 ′. Considering together with the reference example, it is considered that almost all catechins remaining in the first step were extracted in the second step. Moreover, it was 15.79 when the ratio (a / b) of the amino acid (a) and catechin (b) of sample D3 'was calculated.
Figure 0005238993

実施例5.茶抽出物の製造(5:スケールアップ)
本発明の茶抽出物の生産性を検討した。
まず、第一工程としてカラム型抽出機に2.00kgの緑茶葉(火入れ度:弱)を封入し、抽出機上部から25℃のイオン交換水を26.4kg加え、緑茶葉を浸漬させた。そこに25℃のイオン交換水を3.3L/minの流量にて連続的に30分通液し、低温抽出液を得た(試料E1)。次に、第二工程として、通液するイオン交換水温度を85℃に切り替え、3.3L/minの流量にて連続的に60分通液し、高温抽出液得た(試料E2)。その後、第三工程として、試料E2抽出後の抽出残渣に酵素としてプロテアーゼ及びペクチナーゼを各40gずつ添加し、酸化防止剤としてL−アスコルビン酸を6.00g添加し、40℃のイオン交換水を加え総重量32kgに調整し、40℃に保持したまま5.0L/minにて16時間循環通液を行い、酵素反応を行った。得られた酵素処理液を90℃10分加熱し酵素を失活させ、酵素抽出液を得た(試料E3)。さらに第4工程として、上記試料E1と試料E3とを混合し、茶抽出物を得た(試料E4)。
試料E1〜E4について、参考例1と同様にアミノ酸及びカテキン類の含量を分析した。
結果を表7に示す。アミノ酸の含量は、試料E1が18.8g、試料E2が4.5g、試料E3が41.8gであった。一方、カテキン類の含量は、試料E1が67.3g、試料E2が80.0g、試料E3が31.4gであった。
この結果と実施例4とを合わせて考察すると、実施例4と同様、低温抽出液(試料E1)と酵素抽出液(試料E3)でアミノ酸含量が高く、高温抽出液(試料E2)にカテキン類が多く含まれていることが確認され、本発明の製造方法が実生産レベルにおいても問題無く製造可能であることが確認できた。

Figure 0005238993
Example 5 FIG. Production of tea extract (5: scale up)
The productivity of the tea extract of the present invention was examined.
First, as a first step, 2.00 kg of green tea leaves (heating degree: weak) were sealed in a column type extractor, 26.4 kg of 25 ° C. ion exchange water was added from the top of the extractor, and the green tea leaves were immersed. Thereto, 25 ° C. ion exchange water was continuously passed at a flow rate of 3.3 L / min for 30 minutes to obtain a low temperature extract (sample E1). Next, as the second step, the temperature of ion exchange water to be passed was switched to 85 ° C. and passed continuously for 60 minutes at a flow rate of 3.3 L / min to obtain a high temperature extract (sample E2). Thereafter, as a third step, 40 g each of protease and pectinase as enzymes are added to the extraction residue after sample E2 extraction, 6.00 g of L-ascorbic acid is added as an antioxidant, and ion exchange water at 40 ° C. is added. The total weight was adjusted to 32 kg, and circulation reaction was carried out at 5.0 L / min for 16 hours while maintaining the temperature at 40 ° C. to carry out the enzyme reaction. The obtained enzyme treatment liquid was heated at 90 ° C. for 10 minutes to deactivate the enzyme, and an enzyme extract was obtained (sample E3). Further, as a fourth step, the sample E1 and the sample E3 were mixed to obtain a tea extract (sample E4).
Samples E1 to E4 were analyzed for the content of amino acids and catechins in the same manner as in Reference Example 1.
The results are shown in Table 7. The amino acid content was 18.8 g for sample E1, 4.5 g for sample E2, and 41.8 g for sample E3. On the other hand, the content of catechins was 67.3 g for sample E1, 80.0 g for sample E2, and 31.4 g for sample E3.
Considering this result together with Example 4, as in Example 4, the amino acid content is high in the low temperature extract (sample E1) and the enzyme extract (sample E3), and the catechins in the high temperature extract (sample E2). As a result, it was confirmed that the production method of the present invention can be produced without any problems even at the actual production level.
Figure 0005238993

実施例6.茶抽出物(パウダー)の製造
まず、第一工程として、実施例4で得られた混合液(試料D4’)をエバポレーターによりBrix15となるよう濃縮し、濃縮エキスを得た(試料F1)。次に第二工程として、試料F1を凍結乾燥機にてパウダー状にし、緑茶パウダーを得た(試料F2)。次に第三工程として、試料F2にBrix15となるようにイオン交換水を適量加え、還元濃縮エキスを得た(試料F3)。
試料F1および試料F3について、参考例1と同様に、アミノ酸及びカテキン類含量を分析した。また、専門パネラー3名によりその香味評価を実施した。
香味評価の結果、試料F1および試料F3ともに、コクと厚みのある豊かな旨味を有し、苦味・渋味のない嗜好性に優れたものであった。このことより、濃縮エキスを凍結乾燥等の方法によりパウダー化し、さらにそれを再溶解することでも、濃縮エキスの香味が損なわれないことが分かった。
Example 6 Production of tea extract (powder) First, as a first step, the mixed solution (sample D4 ′) obtained in Example 4 was concentrated to Brix15 by an evaporator to obtain a concentrated extract (sample F1). Next, as a second step, the sample F1 was powdered with a freeze dryer to obtain a green tea powder (sample F2). Next, as a third step, an appropriate amount of ion-exchanged water was added to the sample F2 so as to be Brix15 to obtain a reduced concentrated extract (sample F3).
Sample F1 and Sample F3 were analyzed for amino acid and catechin content in the same manner as in Reference Example 1. Moreover, the flavor evaluation was implemented by three special panelists.
As a result of the flavor evaluation, both sample F1 and sample F3 had rich and rich umami taste, and were excellent in palatability without bitterness and astringency. From this, it was found that the flavor of the concentrated extract was not impaired even when the concentrated extract was powdered by a method such as freeze-drying and further dissolved again.

実施例7.茶飲料の製造
実施例3で製造した茶抽出物(試料D4)を用いて茶飲料を製造した。すなわち、緑茶葉45gをニーダーで抽出(80℃、10分)し、遠心分離機ならびにフィルターにて茶葉を分離して緑茶液を得、調合タンクにてこの緑茶液に酸化防止剤(L-アスコルビン酸)2g及び重曹(炭酸水素ナトリウム)2gを添加し、さらに、試料D4を、試料D4由来のアミノ酸量が最終飲料中に20ppmとなるように添加し、最後に純水を加え7Lに調整し調合液とした。そしてこの調合液を、UHT殺菌(130℃、1分)後、500mLのペットボトル容器に充填して容器詰緑茶飲料を得た。また、対照として試料D4を添加しないこと以外は、同様にして、緑茶飲料を得た。この緑茶飲料の香味を評価したところ、試料D4を添加していない緑茶飲料(対照)と比較し、試料D4を添加した緑茶飲料は、複雑な旨みを有し、かつ渋みが抑制された新規な香味特徴を有する緑茶飲料であった。
さらに実施例4で製造した茶抽出物(試料D4’)を用いて同様にして茶飲料を製造した。この茶飲料も、対照と比較して、複雑な旨みを有し、かつ渋みが抑制された新規な香味特徴を有する緑茶飲料であった。
Example 7 Production of tea beverage A tea beverage was produced using the tea extract (sample D4) produced in Example 3. That is, 45 g of green tea leaves were extracted with a kneader (80 ° C., 10 minutes), and the tea leaves were separated with a centrifuge and a filter to obtain a green tea liquid. 2 g of acid) and 2 g of sodium bicarbonate (sodium bicarbonate) are added, and sample D4 is added so that the amount of amino acid derived from sample D4 is 20 ppm in the final beverage, and finally pure water is added to adjust to 7 L. It was set as the preparation liquid. And after preparing this UHT sterilization (130 degreeC, 1 minute), it filled with a 500 mL PET bottle container, and the container-packed green tea drink was obtained. Further, a green tea beverage was obtained in the same manner except that the sample D4 was not added as a control. When the flavor of this green tea beverage was evaluated, the green tea beverage to which the sample D4 was added had a complex taste and a novel astringency was suppressed as compared with the green tea beverage to which the sample D4 was not added (control). It was a green tea beverage with flavor characteristics.
Further, a tea drink was produced in the same manner using the tea extract (sample D4 ′) produced in Example 4. This tea beverage was also a green tea beverage having a new flavor characteristic with a complex taste and astringency suppressed as compared with the control.

参考例の条件により25℃のイオン交換水によって緑茶葉を抽出した際のカテキン類とアミノ酸の抽出傾向を示すグラフである。It is a graph which shows the extraction tendency of catechins and an amino acid at the time of extracting a green tea leaf with 25 degreeC ion-exchange water by the conditions of a reference example.

Claims (6)

茶葉に溶媒を接触させて得られる茶抽出物であって、少なくともテアニンを含むアミノ酸とカテキン類とを含有し、該茶抽出物中の茶葉由来固形分に対する前記アミノ酸の総量の割合が7.0重量%以上であり、前記アミノ酸の総量に対するテアニンの割合が0.10以上0.23以下であり、前記茶抽出物中の茶葉由来固形分に対するカテキン類の総量の割合が15.0重量%以下である、茶抽出物。 A tea extract obtained by bringing a solvent into contact with tea leaves, comprising at least an amino acid containing theanine and catechins, wherein the ratio of the total amount of the amino acids to the solid content derived from tea leaves in the tea extract is 7.0. The ratio of theanine to the total amount of the amino acids is 0.10 to 0.23 , and the ratio of the total amount of catechins to the tea leaf-derived solid content in the tea extract is 15.0% by weight or less. Is a tea extract. アミノ酸の総量に対するテアニンの割合が0.15以上である、請求項1に記載の茶抽出物。 The proportion of theanine against the total amount of amino acids is 0.15 or more, the tea extract according to claim 1. テアニンが、茶葉を40℃以下の溶媒で抽出して得られる茶葉の低温抽出物として添加されたものである、請求項1又は2に記載の茶抽出物。 The tea extract according to claim 1 or 2, wherein theanine is added as a low-temperature extract of tea leaves obtained by extracting tea leaves with a solvent of 40 ° C or lower. 茶抽出物のBrixが、0.1〜20%である、請求項1〜3のいずれか1項に記載の茶抽出物。 The tea extract according to any one of claims 1 to 3, wherein the Brix of the tea extract is 0.1 to 20%. 請求項1−4のいずれか1項に記載の茶抽出物に乾燥操作を行って粉体状とした茶抽出物。 The tea extract which dried the tea extract of any one of Claims 1-4, and was made into powder form. 請求項1〜5のいずれかに記載の茶抽出物を含有する、容器詰茶飲料。 Container-packed tea drink containing the tea extract according to any one of claims 1 to 5.
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